Patent Application
20200199259
Copolymers of tetrafluoroethylene and polyfluorovinyloxy monomers including sulfonyl fluoride pendant groups have been made. See, for example, U.S. Pat. No. 3,282,875 (Connolly), U.S. Pat. No. 3,718,627 (Grot), and U.S. Pat. No. 4,267,364 (Grot). Copolymers of fluorinated olefins and polyfluoroallyloxy sulfonyl fluorides have been made. See, for example, U.S. Pat. No. 4,273,729 (Krespan) and U.S. Pat. No. 8,227,139 (Watakabe), and International Pat. Appl. Pub. No. WO 00/24709 (Farnham et al.). Hydrolysis of the sulfonyl fluoride of these copolymers to form an acid or acid salt provides ionic copolymers, which are also called ionomers.
Certain recently disclosed ionomers are said to have high oxygen permeability. See, for example, U.S. Pat. Appl. Pub. Nos. 2017/0183435 (Ino), 2013/0253157 (Takami), 2013/0245219 (Perry), and 2013/0252134 (Takami), and U.S. Pat. No. 8,470,943 (Watakabe).
While ionomers made from tetrafluoroethylene and polyfluorovinyloxy or polyfluoroallyloxy sulfonyl fluorides monomers are known, certain of these materials are highly crystalline and difficult to disperse in common solvent (e.g., water and alcohol mixtures) at high solid percentages (e.g., at least 20% solids). Achieving high percent solids may be particularly challenging when an ionomer of high equivalent weight is desired. A high solids percentage is useful for making thicker membranes for membrane electrode assemblies. While for some applications thin membranes are desirable (e.g., automotive membranes can be about 12 micrometers thick), other applications require thicker membranes (e.g., greater than 30 micrometers or greater than 50 micrometers). Increasing thickness by using higher percent solids is advantageous over a multi-pass process to build thickness. Furthermore, increasing the solubility in common solvents can obviate the need for using high boiling solvents such as DMF or DMSO and allow for using lower manufacturing temperatures during the manufacturing process of ionomer membranes. Operating at lower coating temperature for the membrane or electrode catalyst particle help protect the overall article of manufacture.
Easy-to-process ionomers with low hydrogen permeation for membrane applications in fuel cells or high oxygen permeation ionomers for electrode applications are also difficult to achieve. Membrane electrode assemblies useful in solid polymer electrolyte fuel cells include electrode catalyst layers including a catalyst (e.g., platinum) and an ionomer. Since the catalysts (e.g., platinum) are typically expensive, decreasing the amount of catalyst can be desirable. For an ionomer used in the electrode, high oxygen permeability is desirable to minimize resistance. In the ionic catalyst layer, it is desirable to have a high oxygen permeability without lowering the ionic conductivity.
The copolymers in the fluoropolymer dispersions of the present disclosure include vinyl ether or allyl ether monomer units in addition to tetrafluoroethylene and sulfonyl group-containing monomer units. Inclusion of such vinyl and allyl ethers can lead to an improved processability profile in common solvents by improving solubility in a dispersion. Inclusion of such monomer units can also typically provide low hydrogen permeation for membrane applications in fuel cells or high oxygen permeation ionomers for electrode applications. The melt flow indexes and equivalent weights of the copolymers typically also provide advantageous mechanical properties and conductivity. In one aspect, the present disclosure provides an aqueous fluoropolymer dispersion of a copolymer including divalent units represented by formula [CF2-CF21]—, divalent units independently represented by formula:
and one or more divalent units independently represented by formula:
In these formulas, a is 0 or 1, b is a number from 2 to 8, c is a number from 0 to 2, e is a number from 1 to 8 with the proviso that when a and c are 0, then e is 3 to 8, Z is independently a hydrogen, alkyl having up to four carbon atoms, an alkali-metal cation, or a quaternary ammonium cation, Rf is a linear or branched perfluoroalkyl group having from 1 to 8 carbon atoms and optionally interrupted by one or more —O— groups, z is 0, 1, or 2, each n is independently from 1, 2, 3, or 4, and m is 0 or 1. The fluoropolymer dispersion comprises at least 10% by weight of the copolymer, based on the total weight of the dispersion, and the copolymer has an —SO3Z equivalent weight in a range from 600 to 2000. A variation of the copolymer in which —SO3Z is replaced with —SO2F has a melt flow index of up to 80 grams per ten minutes measured at a temperature of 265° C. and at a support weight of 5 kg. In some embodiments, the dispersion also contains organic solvent.
In another aspect, the present disclosure provides a method of making a fluoropolymer dispersion. The method includes combining components including water, an organic solvent, and at least 10% by weight of a copolymer, based on the total weight of the components, and mixing the components at ambient temperature and pressure to make the fluoropolymer dispersion. The copolymer includes divalent units represented by formula —[CF2—CF2]—, divalent units independently represented by formula:
and one or more divalent units independently represented by formula:
In these formulas, a is 0 or 1, b is a number from 2 to 8, c is a number from 0 to 2, and e is a number from 1 to 8, Z is independently a hydrogen, alkyl having up to four carbon atoms, an alkali-metal cation, or a quaternary ammonium cation, Rf is a linear or branched perfluoroalkyl group having from 1 to 8 carbon atoms and optionally interrupted by one or more —O— groups, z is 0, 1, or 2, each n is independently from 1, 2, 3, or 4, and m is 0 or 1. The copolymer has an —SO3Z equivalent weight in a range from 600 to 2000.
In this application:
Terms such as “a”, “an” and “the” are not intended to refer to only a singular entity but include the general class of which a specific example may be used for illustration. The terms “a”, “an”, and “the” are used interchangeably with the term “at least one”.
The phrase “comprises at least one of” followed by a list refers to comprising any one of the items in the list and any combination of two or more items in the list. The phrase “at least one of” followed by a list refers to any one of the items in the list or any combination of two or more items in the list.
“Alkyl group” and the prefix “alk-” are inclusive of both straight chain and branched chain groups and of cyclic groups. Unless otherwise specified, alkyl groups herein have up to 20 carbon atoms. Cyclic groups can be monocyclic or polycyclic and, in some embodiments, have from 3 to 10 ring carbon atoms.
The terms “aryl” and “arylene” as used herein include carbocyclic aromatic rings or ring systems, for example, having 1, 2, or 3 rings and optionally containing at least one heteroatom (e.g., 0, S, or N) in the ring optionally substituted by up to five substituents including one or more alkyl groups having up to 4 carbon atoms (e.g., methyl or ethyl), alkoxy having up to 4 carbon atoms, halo (i.e., fluoro, chloro, bromo or iodo), hydroxy, or nitro groups. Examples of aryl groups include phenyl, naphthyl, biphenyl, fluorenyl as well as furyl, thienyl, pyridyl, quinolinyl, isoquinolinyl, indolyl, isoindolyl, triazolyl, pyrrolyl, tetrazolyl, imidazolyl, pyrazolyl, oxazolyl, and thiazolyl.
“Alkylene” is the multivalent (e.g., divalent or trivalent) form of the “alkyl” groups defined above. “Arylene” is the multivalent (e.g., divalent or trivalent) form of the “aryl” groups defined above.
“Arylalkylene” refers to an “alkylene” moiety to which an aryl group is attached. “Alkylarylene” refers to an “arylene” moiety to which an alkyl group is attached.
The terms “perfluoro” and “perfluorinated” refer to groups in which all C—H bonds are replaced by C—F bonds.
The phrase “interrupted by at least one —O— group”, for example, with regard to a perfluoroalkyl or perfluoroalkylene group refers to having part of the perfluoroalkyl or perfluoroalkylene on both sides of the —O— group. For example, —CF2CF2—O—CF2—CF2— is a perfluoroalkylene group interrupted by an —O—.
All numerical ranges are inclusive of their endpoints and nonintegral values between the endpoints unless otherwise stated (e.g., 1 to 5 includes 1, 1.5, 2, 2.75, 3, 3.80, 4, 5, etc.).
The copolymer in the fluoropolymer dispersion according to the present disclosure includes divalent units represented by formula —[CF2—CF2]—. In some embodiments, the copolymer comprises at least 60 mole % of divalent units represented by formula —[CF2—CF2—], based on the total moles of divalent units. In some embodiments, the copolymer comprises at least 65, 70, 75, 80, or 90 mole % of divalent units represented by formula —[CF2—CF2]—, based on the total moles of divalent units. Divalent units represented by formula —[CF2—CF21]— are incorporated into the copolymer by copolymerizing components including tetrafluoroethylene (TFE). In some embodiments, the components to be polymerized include at least 60, 65, 70, 75, 80, or 90 mole % TFE, based on the total moles of components to be polymerized.
The copolymer in the fluoropolymer dispersion according to the present disclosure includes divalent units independently represented by formula:
In this formula, a is 0 or 1, b is a number from 2 to 8, c is a number from 0 to 2, and e is a number from 1 to 8. In some embodiments, b is a number from 2 to 6 or 2 to 4. In some embodiments, b is 2. In some embodiments, e is a number from 1 to 6 or 2 to 4. In some embodiments, e is 2. In some embodiments, e is 4. In some embodiments, c is 0 or 1. In some embodiments, c is 0. In some embodiments, c is 0, and e is 2 or 4. In some embodiments, c is 0, and e is 3 to 8, 3 to 6, 3 to 4, or 4. In some embodiments, when a and c are 0, then e is 3 to 8, 3 to 6, 3 to 4, or 4. In some embodiments, b is 3, c is 1, and e is 2. In some embodiments, a, b, c, and e may be selected to provide greater than 2, at least 3, or at least 4 carbon atoms. CeF2e may be linear or branched. In some embodiments, CeF2e can be written as (CF2)e, which refers to a linear perfluoroalkylene group. When c is 2, the b in the two CbF2b groups may be independently selected. However, within a CbF2b group, a person skilled in the art would understand that b is not independently selected. CbF2b may be linear or branched. In some embodiments, CbF2b can be written as (CF2)b, which refers to a linear perfluoroalkylene group. Also in this formula, each Z is independently a hydrogen, alkyl having up to 4, 3, 2, or 1 carbon atoms, an alkali metal cation, or a quaternary ammonium cation. The quaternary ammonium cation can be substituted with any combination of hydrogen and alkyl groups, in some embodiments, alkyl groups independently having from one to four carbon atoms. In some embodiments, Z is an alkali-metal cation. In some embodiments, Z is a sodium or lithium cation. In some embodiments, Z is a sodium cation. Copolymers having divalent units represented by this formula can be prepared by copolymerizing components including at least one polyfluoroallyloxy or polyfluorovinyloxy compound represented by formula CF2═CF(CF2)a—(OCbF2b)c—O—(CeF2e)—SO—2X″, in which a, b, c, and e are as defined above in any of their embodiments, and each X″ is independently —F, —NZH, or —OZ. Suitable polyfluoroallyloxy and polyfluorovinyloxy compounds of this formula include CF2═CFCF2—O—CF2—SO2X″, CF2═CFCF2—O—CF2CF2—SO2X″, CF2═CFCF2—O—CF2CF2CF2—SO2X″, CF2═CFCF2—O—CF2CF2CF2CF2—SO—X″, CF2═—CFCF2—O—CF2—CF(CF3)—O—(CF2)e—SO2X″, CF2═CF—O—CF2—SO2X″, CF2═CF—O—CF2CF2CF2—SO2X″, CF2═CF—O—CF2CF2CF2—SO2X″, CF2═CF—O—CF2CF2CF2CF2—SO—X″, and CF2═CF—O—CF2—CF(CF3)—O—(CF2)e—SO13 2X″. In some embodiments, the compound represented by formula CF2═CF(CF2)a—(OCbF2b)c—O—CeF2e)—SO2X″ is CF2═CFCF2—O—CF2CF2SO2X″, CF2═CF—O—CF2CF2—SO2X″, CF2═CFCF2—O—CF2CF2CF2CF2—SO2X″, or CF2═CF—O—CF2CF2CF2SO2X″. In some embodiments, the compound represented by formula CF2═CF(CF2)a—(OCbF2b)—O—(CeF2e)—SO2X″ is CF2═CFCF2—O—CF2CF2—SO2X″, CF2═CFCF2—O—CF2CF2CF2CF2—SO2X″, or CF2═CF—O—CF2CF2CF2CF2—SO2X″. In some embodiments, the compound represented by formula CF2═CF(CF2)a—(OCbF2b)c—O—(CeF2e)—SO2X″ is CF2═CFCF2—O—CF2CF2—SO2X″ or CF2═CFCF2—O—CF2CF2CF2CF2—SO2X″.
Compounds represented by formula CF2═CF(CF2)a—(OCbF2b)c—O—CeF2e)—SO2X″ can be made by known methods. For example acid fluorides represented by formula FSO2(CF2)e-1—C(O)F or FSO2(CF2)e—(OCbF2b)c-1—C(O)F can be reacted with perfluoroallyl chloride, perfluoroallyl bromide, or perfluoroallyl fluorosulfate in the presence of potassium fluoride as described in U.S. Pat. No. 4,273,729 (Krespan) to make compounds of formula CF2═CFCF2—(OCbF2b)c—O—(CeF2e)—SO2F. Compounds of formula CF2═CFCF2—(OCbF2b)c—O—(CeF2e)—SO2F can be hydrolyzed with a base (e.g., alkali metal CF2═CFCF2—(OCbF2b)c—O—(CeF2a)—SO3Z.
In some embodiments of the copolymer in the fluoropolymer dispersion according to the present disclosure, at least some of the fluorinated divalent units are derived from at least one short-chain SO2X″-containing vinyl ether monomer. Likewise, short-chain SO2X″-containing vinyl ether monomers may be useful components to be polymerized in the methods according to the present disclosure. Short-chain SO2X″-containing vinyl ether monomers represented by formula CF2═—CF—O—(CF2)2—SO2—X″ (e.g., those represented by formula [CF2═CF—O—(CF2)213 SO3]M, where M is an alkali metal, and CF2═CF—O—(CF2)2—SO2NZH) can be made by known methods. Conveniently, a compound of formula [CF2═CF—O—(CF2)2—SO3]M can be prepared in three steps from the known compound represented by formula FC(O)—CF(CF3)—O—(CF2)2—SO2F. As reported in Gronwald, O., et al; “Synthesis of difluoroethyl perfluorosulfonate monomer and its application”; J. Fluorine Chem., 2008, 129, 535-540, the acid fluoride can be combined with a methanol solution of sodium hydroxide to form the disodium salt, which can be dried and heated in dry diglyme to effect the carboxylation. FC(O)—CF(CF3)—O—(CF2)2—SO2F can be prepared by ring-opening and derivatization of tetrafluoroethane-β-sultone as described in U.S. Pat. No. 4,962,292 (Marraccini et al.). Compounds represented by formula CF2═CF—O—(CF2)a—SO2X″ can also be prepared by hydrolyzing the products from the elimination of halogen from a compound of formula CF2Cl—CFCl—O—(CF2)2—SO2—F described in U.S. Pat. No. 6,388,139 (Resnick) and or hydrolyzing the products of decarboxylation of FSO2—(CF2)3-4—O—CF(CF3)— COO−)pM+P described in U.S. Pat. No. 6,624,328 (Guerra). Compounds of formula CF2═CF—O—(CF2)2—SO2NH2 can be prepared, for example, by reaction of a cyclic sulfone with one equivalent of LHMDS as described by Uematsu, N., et al. “Synthesis of novel perfluorosulfonamide monomers and their application”; J. Fluorine Chem., 2006, 127, 1087-1095.
In some embodiments of the copolymer in the fluoropolymer dispersion according to the present disclosure, the copolymer includes divalent units independently represented by formula
In this formula Rf is a linear or branched perfluoroalkyl group having from 1 to 8 carbon atoms and optionally interrupted by one or more —O— groups, z is 0, 1 or 2, each n is independently from 1 to 4, and m is 0 or 1. In some embodiments, n is 1, 3, or 4, or from 1 to 3, or from 2 to 3, or from 2 to 4. In some embodiments, when z is 2, one n is 2, and the other is 1, 3, or 4. In some embodiments, when a is 1 in any of the formulas described above, for example, n is from 1 to 4, 1 to 3, 2 to 3, or 2 to 4. In some embodiments, n is 1 or 3. In some embodiments, n is 1. In some embodiments, n is not 3. When z is 2, the n in the two CnF2a groups may be independently selected. However, within a C.F211 group, a person skilled in the art would understand that n is not independently selected. CnF2n may be linear or branched. In some embodiments, CnF2n is branched, for example, —CF2—CF(CF3)—. In some embodiments, CnF2n can be written as (CF2)n, which refers to a linear perfluoroalkylene group. In these cases, the divalent units of this formula are represented by formula
In some embodiments, CnF2n is —CF2—CF2—CF2—. In some embodiments, (OCnF2n)z is represented by —O—(CF2)1-4—[O(CF2)1-4]-0-1. In some embodiments, Rf is a linear or branched perfluoroalkyl group having from 1 to 8 (or 1 to 6) carbon atoms that is optionally interrupted by up to 4, 3, or 2 —O— groups. In some embodiments, Rf is a perfluoroalkyl group having from 1 to 4 carbon atoms optionally interrupted by one —O— group. In some embodiments, z is 0, m is 0, and Rf is a linear or branched perfluoroalkyl group having from 1 to 4 carbon atoms. In some embodiments, z is 0, m is 0, and Rf is a branched perfluoroalkyl group having from 3 to 8 carbon atoms.
In some embodiments, m is 1, and Rf is a branched perfluoroalkyl group having from 3 to 8 carbon atoms or a linear perfluoroalkyl group having 5 to 8 carbon atoms. In some embodiments, Rf is a branched perfluoroalkyl group having from 3 to 6 or 3 to 4 carbon atoms. An example of a useful perfluoroalkyl vinyl ether (PAVE) from which these divalent units in which m and z are 0 are derived is perfluoroisopropyl vinyl ether (CF2═CFOCF(CF3)2), also called iso-PPVE. Other useful PAVEs include perfluoromethyl vinyl ether, perfluoroethyl vinyl ether, and perfluoropropyl vinyl ether.
Divalent units represented by formulas
in which m is 0, typically arise from perfluoroalkoxyalkyl vinyl ethers. Suitable perfluoroalkoxyalkyl vinyl ethers (PAOVE) include those represented by formula CF2═CF[O(CF2)n]2ORf and CF2═CF(OCnF2n)2)ORf, in which n, z, and Rf are as defined above in any of their embodiments. Examples of suitable perfluoroalkoxyalkyl vinyl ethers include CF2═CFOCF2OCF3, CF2═CFOCF2OCF2CF3, CF2═CFOCF2CF2OCF3, CF2═CFOCF2CF2CF2OCF3, CF2═CFOCF2CF2CF2CF2OCF3, CF2═CFOCF2CF2OCF2CF2CF3, CF2═CFOCF2CF2CF2OCF2CF3, CF2═CFOCF2CF2CF2CF2OCF2CF3, CF2═CFOCF2CF2OCF2OCF3, CF2═CFOCF2CF2OCF2CF2OCF3, CF2═CFOCF2CF2OCF2CF2CF2OCF3, CF2═CFOCF2CF2OCF2CF2CF2CF2CF2OCF3, CF2═CFOCF2CF2OCF2CF2CF2CF2CF2OCF3, CF2═CFOCF2CF2(OCF2)OCF3, CF2═CFOCF2CF2(OCF2)OCF3, CF2═CFOCF2CF2═CF2OCF2OCF3, CF2═CFOCF2CF2OCF2CF2CF3CF2═CFOCF2CF2OCF2CF2CF2CF3, CF2═CFOCF2CF(CF3)—O—C3F7 (PVVE-2), CF2═CF(OCF2CF(CF3))2)—O—C3F7(PPVE-3), and CF2═CF((OCF2CF(CF3)—O—C3F7(PPVE-4). In some embodiments, the perfluoroalkoxyalkyl vinyl ether is selected from CF2═CFOCF2OCF3, CF2═CFOCF2OCF2CF3, CF2═CFOCF2CF2OCF3, CF2=CFOCF2CF2CF2OCF3, CF2═CFOCF2CF2CF2CF2OCF3, CF2═CFOCF2CF2CF2OCF2CF3, CF2=CFOCF2CF2CF2CF2OCF2CF3, CF2═CFOCF2CF2OCF2OCF3, CF2═CFOCF2CF2OCF2CF2CF2OCF3, CF2═CFOCF2CF2OCF2CF2CF2CF2OCF3, CF2═CFOCF2CF2OCF2CF2CF2CF2CF2OCF3, CF2═CFOCF2CF2(OCF2)3OCF3, CF2═CFOCF2CF2(OCF2)4OCF3, CF2=CFOCF2CF2OCF2OCF2OCF3, and combinations thereof. Many of these perfluoroalkoxyalkyl vinyl ethers can be prepared according to the methods described in U.S. Pat. No. 6,255,536 (Worm et al.) and U.S. Pat. No. 6,294,627 (Worm et al.). In some embodiments, the PAOVE is perfluoro-3-methoxy-n-propyl vinyl ether. In some embodiments, the PAOVE is other than perfluoro-3-methoxy-n-propyl vinyl ether.
The divalent units represented by formula
in which m is 1, are typically derived from at least one perfluoroalkoxyalkyl allyl ether. Suitable perfluoroalkoxyalkyl allyl ethers include those represented by formula CF2═CFCF2(OCnF2n)zORf, in which n, z, and Rf are as defined above in any of their embodiments. Examples of suitable perfluoroalkoxyalkyl allyl ethers include CF2═CFCF2OCF2CF2OCF3, CF2═CFCF2OCF2CF2CF2OCF3, CF2═CFCF2OCF2OCF3, CF2═CFCF2OCF2OCF2CF3, CF2═CFCF2OCF2CF2CF2CF2OCF3, CF2═CFCF2OCF2CF2OCF2CF3, CF2═CFCF2OCF2CF2CF2OCF2CF3, CF2═CFCF2OCF2CF2CF2CF2OCF2CF3, CF2═CFCF2OCF2CF2OCF2OCF3, CF2═CFCF2OCF2CF2OCF2CF2OCF3, CF2═CFCF2OCF2CF2OCF2CF2CF2OCF3, CF2═CFCF2OCF2CF2OCF2CF2CF2CF2OCF3, CF2═CFCF2OCF2CF2OCF2CF2CF2CF2CF2OCF3, CF2═CFCF2OCF2CF2(OCF2)3OCF3, CF2═CFCF2OCF2CF2(OCF2)4OCF3, CF2═CFCF2OCF2CF2OCF2OCF2OCF3, CF2═CFCF2OCF2CF2OCF2CF2CF3, CF2═CFCF2OCF2CF2OCF2CF2OCF2CF2CF3, CF2═CFCF2OCF2CF(CF3)—O—C3F7, and CF2═CFCF2(OCF2CF(CF3))2—O—C3F7. In some embodiments, the perfluoroalkoxyalkyl allyl ether is selected from CF2═CFCF2OCF2CF2OCF3, CF2═CFCF2OCF2CF2CF2OCF3, CF2═CFCF2OCF2OCF3, CF2═CFCF2OCF2OCF2CF3, CF2═CFCF2OCF2CF2CF2CF2OCF3, CF2═CFCF2OCF2CF2OCF2CF3, CF2═CFCF2OCF2CF2CF2OCF2CF3, CF2=CFCF2OCF2CF2CF2CF2OCF2CF3, CF2═CFCF2OCF2CF2OCF2OCF3, CF2═CFCF2OCF2CF2OCF2CF2OCF3, CF2═CFCF2OCF2CF2OCF2CF2CF2OCF3, CF2═CFCF2OCF2CF2OCF2CF2CF2CF2OCF3, CF2═CFCF2OCF2CF2OCF2CF2CF2CF2CF2OCF3, CF2=CFCF2OCF2CF2(OCF2)3OCF3, CF2═CFCF2OCF2CF2(OCF2)4OCF3, CF2═CFCF2OCF2CF2OCF2OCF2OCF3, CF2═CFCF2OCF2CF2OCF2CF2CF3, CF2═CFCF2OCF2CF2OCF2CF2OCF2CF2CF3, and combinations thereof.
Many of these perfluoroalkoxyalkyl allyl ethers can be prepared, for example, according to the methods described in U.S. Pat. No. 4,349,650 (Krespan). Perfluoroalkoxyalkyl allyl ethers can also be prepared by combining first components comprising at least one of CF2═CF—CF2—OSO2Cl or CF2═CF—CF2—OSO2CF3, a polyfluorinated compound comprising at least one ketone or carboxylic acid halide or combination thereof, and fluoride ion. Polyfluorinated compounds comprising at least one ketone or carboxylic acid halide or combination thereof and fluoride ions can be any of those described, for example, in U.S. Pat. No. 4,349,650 (Krespan).
CF2═CF—CF2—OSO2Cl can convenientlhy be prepard by reaction of boron trichloride (BCl3) and ClSO3H to prpvode B(OSO2Cl)3 and subsequently reacting the B(OSO2Cl)3 and hexafluoropropylene (HFP). The reaction of BCl3 and CkSO3H can be carried out, for example, by dropwise addition of neat ClSO3H to gaseous BCl3 at below 50° C. or, in the case of condensed BC3 at sub-ambient temperature. The reaction can be carried out at a temperature of least −20° C., −10° C., 0° C., 10° C., or 20° C. and up to 30° C., 40° C., or 50° C. The addition of ClSO3H to BCl3 can be carried out at a rate, for example, to maintain the temperature of the mixture at 10° C. or below. B(OSO2Cl)3 can be isolated as a white powder after volatile starting materials are removed under vacuum. B(OSO2Cl)3 can then be suspended or dissolved in a solvent, and HFP can be added at below 50° C., in some embodiments, at sub-ambient temperature. For example, the reaction can be carried out at a temperature of least −20° C., −10° C., 0° C., 10° C., or 20° C. and up to 30° C., 40° C., or 50° C. Suitable solvents include halogenated solvents (e.g., methylene chloride or Freon-113). In some embodiments, the solvent is a non-aromatic solvent. CF2═CF—CF2—OSO2Cl can be isolated and optionally purified using conventional methods.
Combining components comprising M(OSO2CF3)3 and hexafluoropropylene (HFP) to provide CF2═CF—CF2—OSO2CF3, wherein M is Al or B. Al(OSO2CF3)3 is commercially available, for example, from chemical suppliers such as abcr GmbH (Karlsruhe, Germany) and Sigma-Aldrich (St. Louis, Miss.). Reaction of BCl3 and CF3SO3H can be useful to provide B(OSO2CF3)3. The reaction of BCl3 and CF3SO3H can be carried out, for example, by dropwise addition of neat CF3SO3H to gaseous BCl3 at below 50° C. or, in the case of condensed BCl3 at sub-ambient temperature. The reaction can be carried out at a temperature of least −20° C., −10° C., 0° C., 10° C., or 20° C. and up to 30° C., 40° C., or 50° C. The addition of CF3SO3H to BCl3 can be carried out at a rate, for example, to maintain the temperature of the mixture at 10° C. or below. B(OSO2CF3)3 can be isolated as a white powder after volatile starting materials are removed under vacuum.
B(OSO2CF3)3 can combined with HFP at a temperature above 0° C. In some embodiments, the reaction can be carried out at a temperature up to 50° C., 40° C., 30° C., 20° C., or 10° C. The reaction can be carried out at a temperature in a range from above 0° C. to 10° C., in some embodiments, in a range from 2° C. to 10° C., and in some embodiments, in a range from 4° C. to 8° C. The reaction mixture is combined with water at a temperature below 28° C., in some embodiments, in a range from above 25° C. to 27° C. The reaction product can then be isolated and optionally purified using conventional methods (e.g., separation of the organic fraction, drying over a drying agent, filtering, and distilling). The product CF2═CF—CF2OSO2CF3 can be isolated in 75% yield, which is an improvement over the yield reported in Petrov, V. A., J. Fluorine Chem. 1995, 73, 17-19.
The vinyl ethers and allyl ethers described above in any of their embodiments, may be present in the components to be polymerized in any useful amount, in some embodiments, in an amount of up to 20, 15, 10, 7.5, or 5 mole percent, of at least 3, 4, 4.5, 5, or 7.5 mole percent, or in a range from 3 to 20, 4 to 20, 4.5 to 20, 5 to 20, 7.5 to 20, or 5 to 15 mole percent, based on the total amount of polymerizable components. Accordingly, the copolymer in the fluoropolymer dispersion according to the present disclosure can include divalent units derived from these vinyl ethers and allyl ethers in any useful amount, in some embodiments, in an amount of up to 20, 15, 10, 7.5, or 5 mole percent, of at least 3, 4, 4.5, 5, or 7.5 mole percent, or in a range from 3 to 20, 4 to 20, 4.5 to 20, 5 to 20, 7.5 to 20, or 5 to 15 mole percent, based on the total moles of divalent units.
In some embodiments of the copolymer in the fluoropolymer dispersion according to the present disclosure, the copolymer includes divalent units derived from at least one fluorinated olefin independently represented by formula C(R)2═CF—Rf2. These fluorinated divalent units are represented by formula —[CR2—-CFRf2]−. In formulas C(R)2═CF—Rf2 and —[CR2—CFRf2]—, Rf2 is fluorine or a perfluoroalkyl having from 1 to 8, in some embodiments 1 to 3, carbon atoms, and each R is independently hydrogen, fluorine, or chlorine. Some examples of fluorinated olefins useful as components of the polymerization include, hexafluoropropylene (HFP), trifluorochloroethylene (CTFE), and partially fluorinated olefins (e.g., vinylidene fluoride (VDF), tetrafluoropropylene (R1234yf), pentafluoropropylene, and trifluoroethylene). In some embodiments, the copolymer includes at least one of divalent units derived from chlorotrifluoroethylene or divalent units derived from hexafluoropropylene.
Divalent units represented by formula —[CR2—CFRf2]— may be present in the copolymer in any useful amount, in some embodiments, in an amount of up to 10, 7.5, or 5 mole percent, based on the total moles of divalent units.
In some embodiments of the copolymer in the fluoropolymer dispersion according to the present disclosure, the copolymer is essentially free of VDF units, and the components to be copolymerized are essentially free of VDF. For example, at a pH higher than 8, VDF may undergo dehydrofluorination, and it may be useful to exclude VDF from the components to be polymerized. “Essentially free of VDF” can mean that VDF is present in the components to be polymerized at less than 1 (in some embodiments, less than 0.5, 0.1, 0.05, or 0.01) mole percent. “Essentially free of VDF” includes being free of VDF. Copolymers in the fluoropolymer dispersion of the present disclosure can comprise divalent units independently represented by formula:
wherein p is 0 or 1, q is 2 to 8, r is 0 to 2, s is 1 to 8, and Z′ is a hydrogen, an alkali-metal cation or a quaternary ammonium cation. In some embodiments, q is a number from 2 to 6 or 2 to 4. In some embodiments, q is 2. In some embodiments, s is a number from 1 to 6 or 2 to 4. In some embodiments, s is 2. In some embodiments, s is 4. In some embodiments, r is 0 or 1. In some embodiments, r is 0. In some embodiments, r is 0, and s is 2 or 4. In some embodiments, q is 3, r is 1, and s is 2. CsF2s may be linear or branched. In some embodiments, CsF2s can be written as (CF2)s, which refers to a linear perfluoroalkylene group. When r is 2, the q in the two CqF2q groups may be independently selected. However, within a CqF2q group, a person skilled in the art would understand that q is not independently selected. Each Z′ is independently a hydrogen, an alkali metal cation, or a quaternary ammonium cation. The quaternary ammonium cation can be substituted with any combination of hydrogen and alkyl groups, in some embodiments, alkyl groups independently having from one to four carbon atoms. In some embodiments, Z′ is an alkali-metal cation. In some embodiments, Z′ is a sodium or lithium cation. In some embodiments, Z′ is a sodium cation. Divalent units represented by formula
may be present in the copolymer in any useful amount, in some embodiments, in an amount of up to 10, 7.5, or 5 mole percent, based on the total moles of divalent units.
Copolymers in the fluoropolymer dispersion of the present disclosure can also include units derived from bisolefins represented by formula X2C═CY—(CW2)m—(O)n—RF—(O),—(CW2)p—CY═CX2. In this formula, each of X, Y, and W is independently fluoro, hydrogen, alkyl, alkoxy, polyoxyalkyl, perfluoroalkyl, perfluoroalkoxy or perfluoropolyoxyalkyl, m and p are independently an integer from 0 to 15, and n, o are independently 0 or 1. In some embodiments, X, Y, and W are each independently fluoro,
CF3, C2F5, C3F7, C4F9, hydrogen, CH3, C2H5, C3H7, C4H9. In some embodiments, X, Y, and W are each fluoro (e.g., as in CF2═CF—O—RF—O—CF═CF2 and CF2═CF—CF2—O—RF—O—CF2—CF═CF2). In some embodiments, n and o are 1, and the bisolefins are divinyl ethers, diallyl ethers, or vinyl-allyl ethers. RF represents linear or branched perfluoroalkylene or perfluoropolyoxyalkylene or arylene, which may be non-fluorinated or fluorinated. In some embodiments, RF is perfluoroalkylene having from 1 to 12, from 2 to 10, or from 3 to 8 carbon atoms. The arylene may have from 5 to 14, 5 to 12, or 6 to 10 carbon atoms and may be non-substituted or substituted with one or more halogens other than fluoro, perfluoroalkyl (e.g. —CF3 and —CF2CF3), perfluoroalkoxy (e.g. —O—CF3, —OCF2CF3), perfluoropolyoxyalkyl (e.g., —OCF2OCF3; —CF2OCF2OCF3), fluorinated, perfluorinated, or non-fluorinated phenyl or phenoxy, which may be substituted with one or more perfluoroalkyl, perfluoroalkoxy, perfluoropolyoxyalkyl groups, one or more halogens other than fluoro, or combinations thereof. In some embodiments, RF is phenylene or mono-, di-, tri- or tetrafluoro-phenylene, with the ether groups linked in the ortho, para or meta position. In some embodiments, RF is CF2; (CF2)q wherein q is 2, 3, 4, 5, 6, 7 or 8; CF2—O—CF2; CF2—O—CF2—CF2; CF(CF3)CF2; (CF2)2—O—CF(CF3)—CF2; CF(CF3)—CF2—O—CF(CF3)CF2; or (CF2)2—O—CF(CF3)—CF2—O—CF(CF3)—CF2—O—CF(CF3)—CF2—O—CF2. The bisolefins can introduce long chain branches as described in U.S. Pat. Appl. Pub. No. 2010/0311906 (LavaHee et al.). The bisolefins, described above in any of their embodiments, may be present in the components to be polymerized in any useful amount, in some embodiments, in an amount of up to 2, 1, or 0.5 mole percent and in an amount of at least 0.1 mole percent, based on the total amount of polymerizable components.
Copolymers in the fluoropolymer dispersions of the present disclosure can also include units derived from non-fluorinated monomers. Examples of suitable non-fluorinated monomers include ethylene, propylene, isobutylene, ethyl vinyl ether, vinyl benzoate, ethyl allyl ether, cyclohexyl allyl ether, norbornadiene, crotonic acid, an alkyl crotonate, acrylic acid, an alkyl acrylate, methacrylic acid, an alkyl methacrylate, and hydroxybutyl vinyl ether. Any combination of these non-fluorinated monomers may be useful. In some embodiments, the components to be polymerized further include acrylic acid or methacrylic acid, and the copolymer in the fluoropolymer dispersion of the present disclosure includes units derived from acrylic acid or methacrylic acid. Typically, the copolymer in the fluoropolymer dispersion of the present disclosure does not include cyclic structures comprising fluorinated carbon atoms and oxygen atoms in the main chain (that is, divalent units comprising such cyclic structures).
In some embodiments, the copolymer in the fluoropolymer dispersion of the present disclosure can be made from the sulfonyl fluoride compounds, where X″ in any of the aforementioned compounds represented by formula CF2═CF(CF2)a—(OCbF2b)c—O—(CeF2e)—SO2X″ is F, according to the methods described below, for example. Hydrolysis of a copolymer having —SO2F groups with an alkaline hydroxide (e.g. LiOH, NaOH, or KOH) solution provides —SO3Z groups, which may be subsequently acidified to SO3H groups. Treatment of a copolymer having —SO2F groups with water and steam can form SO3H groups. Thus, copolymers of the present disclosure having —SO2F groups (that is, in which X is F) are useful intermediates for making other copolymers of the present disclosure.
In some embodiments, the method according to the present disclosure includes copolymerizing components including at least one compound represented by formula CF2═CF(CF2)a—(OCbF2b)c—O—(CeF2e)—SO3Z, in which Z, b, c, and e are as defined above in any of their embodiments. In some embodiments, Z is an alkali-metal cation. In some embodiments, Z is a sodium or lithium cation. In some embodiments, Z is a sodium cation. In some embodiments, the compound represented by formula CF2═CF(CF2)a—(OCbF2b)c—O—(CeF2e)—SO3Z is CF2═CFCF2—O—CF2CF2—SO3Na.
The copolymer in the fluoropolymer dispersion according to the present disclosure can have an —SO3Z equivalent weight of up to 2000, 1900, 1800, or 1750. In some embodiments, the copolymer has an —SO3Z equivalent weight of at least 600, 700, 800, 900, 950, or 1000. In some embodiments, the copolymer has an SO3Z equivalent weight in a range from 600 to 2000, 800 to 2000, 950 to 2000, or 1000 to 2000. In general, the —SO3Z equivalent weight of the copolymer refers to the weight of the copolymer containing one mole of —SO3Z groups, wherein Z is as defined above in any of its embodiments. In some embodiments, the—SO3Z equivalent weight of the copolymer refers to the weight of the copolymer that will neutralize one equivalent of base. In some embodiments, the —SO3Z equivalent weight of the copolymer refers to the weight of the copolymer containing one mole of sulfonate groups (i.e., —SO3−). Decreasing the —SO3Z equivalent weight of the copolymer tends to increase proton conductivity in the copolymer but tends to decrease its crystallinity, which may compromise the mechanical properties of the copolymer (e.g., tensile strength). Thus, the —SO3Z equivalent weight of the copolymer in the fluoropolymer dispersion of the present disclosure typically and advantageously provides a balance of the requirements for the electrical and mechanical properties of the copolymer. Equivalent weight can be calculated from the molar ratio of monomer units in the copolymer using, for example, the equation shown in the Examples, below.
The copolymer in the fluoropolymer dispersion of the present disclosure can have up to 30 mole percent of divalent units represented by formula
based on the total amount of the divalent units. In some embodiments, the copolymer comprises up to 25 or 20 mole percent of these divalent units, based on the total amount of these divalent units. The components that are copolymerized in the methods described herein can comprise up to 30 mole percent of at least one compound represented by formula CF2═CF(CF2)a—(OCbF2b)c—O—(CeF2e)—SO2X″, in any of their embodiments described above, based on the total amount of components. In some embodiments, the components comprise up to 25 or 20 mole percent of a compound represented by formula CF2═CF(CF2)a—(OCbF2b)c—O—(CeF2e)—SO2X″, based on the total amount of components.
The molecular weights of copolymers in fluoropolymer dispersions according to the present disclosure can be characterized by the melt viscosity or the melt flow index (MFI, e.g., 265° C./5 kg) of a variation of the copolymer in which —SO3Z is replaced with —SO2F. In some embodiments, the copolymer in the fluoropolymer dispersion of the present disclosure has an MFI of up to 80 grams per 10 minutes, 70 grams per 10 minutes, 60 grams per 10 minutes, 50 grams per 10 minutes, 40 grams per 10 minutes, 30 grams per 10 minutes, or 20 grams per 10 minutes. In some embodiments, the copolymer in the fluoropolymer dispersion according to the present disclosure has an MFI of up to 15 grams per 10 minutes or up to 12 grams per 10 minutes. When the MFI is up to 80, 70, 60, 50, 40, 30, 20, 15, or 12 grams per 10 minutes, good mechanical properties are achieved. The MFI of the copolymer can be affected by adjusting the amount of the initiator and/or chain-transfer agent used during polymerization, both of which affect the molecular weight and molecular-weight distribution of the copolymer. MFI can also be controlled by the rate of addition of initiator to the polymerization. Variations in the monomer composition can also affect the MFI. For the purposes of the present disclosure, MFI is measured according to the test method described in the Examples, below. It should be noted that an MFI of about 20 grams per 10 minutes measured at 270° C./2.16 kg will give an MFI of 43 grams per 10 minutes measured at 265° C./5 kg. In general, when an MFI is measured at 265° C./5 kg, a value of more than twice than an MFI measured at 270° C./2.16 kg is obtained.
Copolymers in the fluoropolymer dispersions of the present disclosure are generally considered ionomers. lonomers typically exhibit a thermal transition between a state in which the ionic clusters are closely associated and a state in which the interactions between those clusters have been weakened. This transition is described as an alpha transition, and the transition temperature is T(α). lonomers with higher T(α) typically have greater mechanical integrity at elevated temperatures than corresponding materials with lower T(α). As a result, to obtain high service temperatures for an ionomer, a relatively high T(α) can be desirable for ionomers. In some embodiments, the a-dispersion temperature T(α) of copolymers in the fluoropolymer dispersion of the present disclosure is at least 95° C., 100° C., 105° C., 110° C., or 115° C. However, we have found that decreasing the T(α) can increase oxygen permeability and that selecting a T(α) to obtain a balance of mechanical integrity and oxygen permeability can be useful. In some embodiments, the a-dispersion temperature [T(α)] of copolymer of the present disclosure is up to 110° C., 105° C., or 100° C., or less than 100° C., in some embodiments, up to 99.5° C. or 99° C. In some embodiments, the α-dispersion temperature [T(α)] of copolymer of the present disclosure is at least room temperature (e.g., 25° C.), in some embodiments, at least 60° C., 65° C., 70° C., 75° C., 80° C., 85° C., 90° C., or 95° C. In some embodiments, the a-dispersion temperature [T(aα] of copolymer of the present disclosure is in a range from 60° C. to 100° C., 70° C. to 100° C., 80° C. to 100° C., 90° C. to 100° C., or 95° C. to 100° C. In some embodiments, the a-dispersion temperature [T(α)] of copolymer of the present disclosure is in a range from 60° C. to 99.5° C., 70° C. to 99.5° C., 80° C. to 99.5° C., 90° C. to 99.5° C., or 95° C. to 99.5° C. In some embodiments, the a-dispersion temperature [T(α)] of copolymer of the present disclosure is in a range from 60° C. to 99° C., 70° C. to 99° C., 80° C. to 99° C., 90° C. to 99° C., or 95° C. to 99° C. In the copolymers of the present disclosure, various factors can affect the [T(α)]. For example, when a, b, c, and e are selected to provide greater than 2, at least 3, or at least 4 carbon atoms in the side chain of the sulfonyl-substituted divalent units a T(α) up to 100° C. (e.g., in a range from 80° C. to 100° C., 90° C. to 100° C., or 95° C. to 100° C.) may be achieved. Also, when m, m′, n, z, Rf, and Rfi are selected to provide greater than 2, at least 3, or at least 4 carbon atoms and/or at least one or 2 oxygen atoms in the side chain of the divalent units represented by formula
a T(α) up to 100° C. (e.g., in a range from 80° C. to 100° C., 90° C. to 100° C., or 95° C. to 100° C.) may be achieved. Including more than 3, 4, 4.5, 5, or 7.5 mol percent of these divalent units can be useful for achieving a T(α) in these ranges. Also, the cation present in the ionomer affects the T(α). Thus, T(α) in the copolymer of the present disclosure can be changed, for example, by ion exchange.
Dynamic mechanical analysis (DMA) is a useful tool for measuring T(α), as polymer physical property changes accompany this transition. The DMA sample cell may be set up in torsion, compression, or tension. For the purposes of this disclosure, T(α) is measured by the method described in the Examples, below. Since the T(α) changes with different cations, for the purposes of this disclosure, the T(α) is understood to be the T(α) when Z is hydrogen.
The glass transition temperature (Tg) is typically defined as the temperature at which an amorphous polymer or amorphous region within a polymer transitions from a glassy material (below Tg) to a rubbery one (above Tg). Gas diffusion rates are correlated to free volume in a polymer [see, for example, Diffusion in Polymers, Marcel Dekker (New York), 1996, edited by P. Neogi]. The free volume increases with temperature, particularly so above the Tg of the polymer. The molecular transport of a gas is enhanced the more the temperature of operation exceeds the Tg of the polymer. As a result, polymers having a relatively low Tg can be desirable for applications in which gas diffusion is required. In some embodiments, in the copolymers in the fluoropolymer dispersions of the present disclosure, a, b, c, and e may be selected to provide greater than 2, at least 3, or at least 4 carbon atoms in the side chain of the sulfonyl-substituted divalent units to achieve a lower Tg. In some embodiments, the variation of the copolymer in which αSO3Z is replaced with —SO2F has a Tg less than 30° C., less than room temperature, or up to 25° C., 20° C., 15° C., or 10° C. Since multiple bulk physical properties of the polymer are different in the glassy state relative to the rubbery state, a variety of methods can be used to measure the Tg. Differential scanning calorimetry (DSC) and dilatometry detect changes in the heat capacity and thermal expansion of the polymer in the two states, while methods such as thermal mechanical analysis
(TMA) and dynamic mechanic analysis (DMA) detect differences in the physical properties in the two states. For the purposes of this disclosure, Tg is measured by the method described in the Examples, below.
In some embodiments, the copolymer in the fluoropolymer dispersion of the present disclosure has at least one of a relative high T(α) (e.g., at least 100° C., 105° C., 110° C., 115° C., 120° C., or 125° C.) or a relative low Tg (e.g., up to 25° C., 20° C., 15° C., or 10° C. as measured for a variation of the copolymer in which —SO3Z is replaced with —SO2F). In some embodiments, the copolymer of the present disclosure has at least one of a relative low T(α) (e.g., up to 110° C., 105° C., 100° C., 99.5° C., or 99° C.) or a relative low Tg (e.g., up to 25° C., 20° C., 15° C., or 10° C.). In some embodiments, the copolymer of the present disclosure has both a relative high T(α) (e.g., at least 100° C., 105° C., 110° C., 115° C., 120° C., or 125° C.) and a relative low Tg (e.g., up to 25° C., 20° C., 15° C., or 10° C. as measured for the variation of the copolymer in which —SO3Z is replaced with —SO2F). In some embodiments, the copolymer of the present disclosure has both a relative low T(α) (e.g., up to 110° C., 105° C., 100° C., 99.5° C., or 99° C.) and a relative low Tg (e.g., up to 25° C., 20° C., 15° C., or 10° C.).
High oxygen permeability in the copolymers disclosed herein can be useful to improve the efficiency of fuel cells, for example. Copolymers in the fluoropolymer dispersions according to the present disclosure typically have useful oxygen permeabilities for fuel cell applications. Oxygen permeability can be measured by methods known in the art including the time lag method described in the Examples, below. As shown in comparison of Example 1 and Comparative Example A below, the addition of the divalent unit represented by formula
can quadruple the oxygen permeability of a copolymer in comparison to a comparable copolymer that does not include these units. Comparable can mean similar to the copolymer of the present disclosure in equivalent weight. When z is 1 or 2, the addition of the divalent unit represented by formula
unexpectedly can increase the oxygen permeability of a copolymer by an order of magnitude in comparison to a comparable copolymer that does not include these units. Thus, when z is 1 or 2, the addition of the divalent unit represented by formula
unexpectedly can increase the oxygen permeability of a copolymer to a greater extent than when z is 0.
The methods of making the copolymer can be carried out by free-radical polymerization. Conveniently, in some embodiments, the methods of making the copolymer in the fluoropolymer dispersion disclosed herein includes radical aqueous emulsion polymerization.
In some embodiments of the method of making the copolymer, a water-soluble initiator (e.g., potassium permanganate or a peroxy sulfuric acid salt) can be useful to start the polymerization process. Salts of peroxy sulfuric acid, such as ammonium persulfate or potassium persulfate, can be applied either alone or in the presence of a reducing agent, such as bisulfites or sulfinates (e.g., fluorinated sulfinates disclosed in U.S. Pat. Nos. 5,285,002 and 5,378,782, both to Grootaert) or the sodium salt of hydroxy methane sulfinic acid (sold under the trade designation “RONGALIT”, BASF Chemical Company, N.J., USA). The choice of initiator and reducing agent, if present, will affect the end groups of the copolymer. The concentration range for the initiators and reducing agent can vary from 0.001% to 5% by weight based on the aqueous polymerization medium.
In some embodiments of the method of making the copolymer, —SO2X″ end groups are introduced in the copolymers according to the present disclosure by generating SO3− radicals during the polymerization process. When salts of peroxy sulfuric acid are used in the presence of a sulfite or bisulfite salt (e.g., sodium sulfite or potassium sulfite), SO3− radicals are generated during the polymerization process, resulting in —SO3− end groups. It might be useful to add metal ions to catalyze or accelerate the formation of —SO3− radicals. By altering the stoichiometry of the sulfite or bisulfite salt versus the peroxy sulfuric acid salt, one can vary the amount of —SO2X″ end groups.
Most of the initiators described above and any emulsifiers that may be used in the polymerization have an optimum pH-range where they show most efficiency. Also, a pH can be selected for the method according to the present disclosure such that the polymerization is carried out with the salt form of the compound of formula CF2═CF(CF2)a═(OCbF2b)c—O—(CeF2e)—SO3Z′, wherein Z′ is an alkali metal cation or an ammonium cation, and to maintain the salt form of the copolymer. For these reason, buffers may be useful. Buffers include phosphate, acetate, or carbonate (e.g., (NH4)2CO3 or NaHCO3) buffers or any other acid or base, such as ammonia or alkali-metal hydroxides. In some embodiments, the copolymerizing is carried out at a pH of at least 8, higher than 8, at least 8.5, or at least 9. The concentration range for the initiators and buffers can vary from 0.01% to 5% by weight based on the aqueous polymerization medium. In some embodiments, ammonia is added to the reaction mixture in an amount to adjust the pH to at least 8, higher than 8, at least 8.5, or at least 9.
Typical chain-transfer agents like H2, lower alkanes, alcohols, ethers, esters, and CH2C12 may be useful in the preparation of the copolymer and ionomer according to the present disclosure. Termination primarily via chain-transfer results in a polydispersity of about 2.5 or less. In some embodiments of the method according to the present disclosure, the polymerization is carried out without any chain-transfer agents. A lower polydispersity can sometimes be achieved in the absence of chain-transfer agents. Recombination typically leads to a polydispersity of about 1.5 for small conversions.
Useful polymerization temperatures can range from 20° C. to 150° C. Typically, polymerization is carried out in a temperature range from 30° C. to 120° C., 40° C. to 100° C., or 50° C. to 90° C. The polymerization pressure is usually in the range of 0.4 MPa to 2.5 MPa, 0.6 to 1.8 MPa, 0.8 MPa to 1.5 MPa, and in some embodiments is in the range from 1.0 MPa to 2.0 MPa. Fluorinated monomers such as HFP can be precharged and fed into the reactor as described, for example, in Modern Fluoropolymers, ed. John Scheirs, Wiley & Sons, 1997, p. 241. Perfluoroalkoxyalkyl vinyl ethers represented by formula CF2═CF(OCnF2n)zORF and perfluoroalkoxyalkyl allyl ethers represented by formula CF2═CFCF2(OCnF2n)2ORf, wherein n, z, and Rf are as defined above in any of their embodiments, are typically liquids and may be sprayed into the reactor or added directly, vaporized, or atomized.
Conveniently, in some embodiments of the method of making the copolymer, the polymerization process may be conducted with no emulsifier (e.g., no fluorinated emulsifier). Surprisingly, we have found that even with the incorporation of liquid perfluoroalkoxyalkyl vinyl or perfluoroalkoxyalkyl allyl ethers or bisolefins in larger amounts, no fluorinated emulsifier is needed to ensure proper incorporation of these monomers. It can be useful to feed the compound represented by formula CF2═CF(CF2)a—(OCbF2b)c—O—(CeF2n)—SO2X″ and the non-functional comonomers (e.g., perfluoroalkoxyalkyl vinyl or perfluoroalkoxyalkyl allyl ethers or bisolefins) as a homogenous mixture to the polymerization. In some embodiments, it is possible to hydrolyze some of the CF2═CF(CF2)a—(OCbF2b)c—O—(CeF2e)—SO2F (e.g., up to 5 ppm) to obtain an “in situ”-emulsifier. Advantageously, this method may be conducted in the absence of any other fluorinated emulsifiers.
In some embodiments, however, perfluorinated or partially fluorinated emulsifiers may be useful. Generally these fluorinated emulsifiers are present in a range from about 0.02% to about 3% by weight with respect to the polymer. Polymer particles produced with a fluorinated emulsifier typically have an average diameter, as determined by dynamic light scattering techniques, in range of about 10 nanometers (nm) to about 500 nm, and in some embodiments in range of about 50 nm to about 300 nm. Examples of suitable emulsifiers include perfluorinated and partially fluorinated emulsifier having the formula [Rf—O—L—COO−]iX1+ wherein L represents a linear partially or fully fluorinated alkylene group or an aliphatic hydrocarbon group, Rf represents a linear partially or fully fluorinated aliphatic group or a linear partially or fully fluorinated aliphatic group interrupted with one or more oxygen atoms, Xi30 represents a cation having the valence i and i is 1, 2 or 3. (See, e.g., U.S. Pat. No. 7,671,112 to Hintzer et al.). Additional examples of suitable emulsifiers also include perfluorinated polyether emulsifiers having the formula CF3—(OCF2)x—O—CF2X′, wherein x has a value of 1 to 6 and X′ represents a carboxylic acid group or salt thereof, and the formula CF3—O—(CF2)3—(OCFCF(CF3)—CF2)y—O—L—Y′ wherein y has a value of 0, 1, 2 or 3, L represents a divalent linking group selected from —CF(CF3)—, —CF2—, and —CF2CF2—, and Y′ represents a carboxylic acid group or salt thereof (See, e.g., U.S. Pat. Publ. No. 2007/0015865 to Hintzer et al.). Other suitable emulsifiers include perfluorinated polyether emulsifiers having the formula Rf-0(CF2CF2O)CF2COOA wherein Rf is CbF(2b+i); where b is 1 to 4, A is a hydrogen atom, an alkali metal or NH4, and x is an integer of from 1 to 3. (See, e.g., U.S. Pat. Publ. No. 2006/0199898 to Funaki et al.). Suitable emulsifiers also include perfluorinated emulsifiers having the formula
F(CF2)bO(CF2CF2O)XCF2COOA wherein A is a hydrogen atom, an alkali metal or NH4, b is an integer of from 3 to 10, and x is 0 or an integer of from 1 to 3. (See, e.g., U.S. Pat. Publ. No. 2007/0117915 to Funaki et al.). Further suitable emulsifiers include fluorinated polyether emulsifiers as described in U.S. Pat. No. 6,429,258 to Morgan et al. and perfluorinated or partially fluorinated alkoxy acids and salts thereof wherein the perfluoroalkyl component of the perfluoroalkoxy has 4 to 12 carbon atoms, or 7 to 12 carbon atoms. (See, e.g., U.S. Pat. No. 4,621,116 to Morgan). Suitable emulsifiers also include partially fluorinated polyether emulsifiers having the formula [Rf—(O)i—CHF—(CF2)x—COO—]iXi+ wherein Rf represents a partially or fully fluorinated aliphatic group optionally interrupted with one or more oxygen atoms, t is 0 or 1 and xis 0 or 1, Xi+ represents a cation having a valence i and i is 1, 2 or 3. (See, e.g., U.S. Pat. Publ. No. 2007/0142541 to Hintzer et al.). Further suitable emulsifiers include perfluorinated or partially fluorinated ether-containing emulsifiers as described in U.S. Pat. Publ. Nos. 2006/0223924, 2007/0060699, and 2007/0142513 each to Tsuda et al. and 2006/0281946 to Morita et al. Fluoroalkyl, for example, perfluoroalkyl carboxylic acids and salts thereof having 6-20 carbon atoms, such as ammonium perfluorooctanoate (APFO) and ammonium perfluorononanoate (see, e.g., U.S. Pat. No. 2,559,752 to Berry) may also be useful. Conveniently, in some embodiments, the method of making the copolymer according to the present disclosure may be conducted in the absence of any of these emulsifiers or any combination thereof.
If fluorinated emulsifiers are used, the emulsifiers can be removed or recycled from the fluoropolymer latex, if desired, as described in U.S. Pat. No. 5,442,097 to Obermeier et al., U.S. Pat. No. 6,613,941 to Felix et al., U.S. Pat. No. 6,794,550 to Hintzer et al., U.S. Pat. No. 6,706,193 to Burkard et al., and U.S. Pat. No. 7,018,541 to Hintzer et al.
In some embodiments, the obtained copolymer latices are purified by at least one of anion- or cation-exchange processes to remove functional comonomers, anions, and/or cations before coagulation or spray drying (described below). As used herein, the term “purify” refers to at least partially removing impurities, regardless of whether the removal is complete. Anionic species that may constitute impurities include, for example, fluoride, anionic residues from surfactants and emulsifiers (e.g., perfluorooctanoate), and residual compounds represented by formula CF2═CF(CF2)a—(OCF2b)c—O—(CeF2e)—SO3Z. It should be noted, however, that it may be desirable to not remove ionic fluoropolymer from the dispersion. Useful anion exchange resins typically comprise a polymer (typically crosslinked) that has a plurality of cationic groups (e.g., quaternary alkyl ammonium groups) paired with various anions (e.g., halide or hydroxide). Upon contact with the fluoropolymer dispersion, anionic impurities in the dispersion become associated with the anion exchange resin. After the anion exchange step, the resultant anion-exchanged dispersion is separated from the anion exchange resin, for example, by filtration. It was reported in U.S. Pat. No. 7,304,101 (Hintzer et al.) that the anionic hydrolyzed fluoropolymer does not appreciably become immobilized on the anion exchange resin, which would lead to coagulation and/or material loss. Anionic exchange resins are available commercially from a variety of sources. If the anion exchange resin is not in the hydroxide form it may be at least partially or fully converted to the hydroxide salt form before use. This is typically done by treating the anion exchange resin with an aqueous ammonia or sodium hydroxide solution. Typically, better yields are obtained using gel-type anion-exchange resins than with macroporous anion exchange resins.
Examples of cationic impurities resulting from the abovementioned polymerization include one or more of, alkali metal cation(s) (e.g., Li+, Na+, K+), ammonium, quaternary alkyl ammonium, alkaline earth cations (e.g., Mg2+, Ca2+), manganese cations (e.g. Mn2+), and Group III metal cations. Useful cation exchange resins include polymers (typically cross-linked) that have a plurality of pendant anionic or acidic groups such as, for example, polysulfonates or polysulfonic acids, polycarboxylates or polycarboxylic acids. Examples of useful sulfonic acid cation exchange resins include sulfonated styrene-divinylbenzene copolymers, sulfonated crosslinked styrene polymers, phenol-formaldehyde-sulfonic acid resins, and benzene-formaldehyde-sulfonic acid resins. Carboxylic acid cation exchange resin is an organic acid, cation exchange resin, such as carboxylic acid cation exchange resin. Cation exchange resins are available commercially from a variety of sources. Cation exchange resins are commonly supplied commercially in either their acid or their sodium form. If the cation exchange resin is not in the acid form (i.e., protonated form) it may be at least partially or fully converted to the acid form in order to avoid the generally undesired introduction of other cations into the dispersion. This conversion to the acid form may be accomplished by means well known in the art, for example by treatment with any adequately strong acid.
If purification of the fluoropolymer dispersion is carried out using both anion and cation exchange processes, the anion exchange resin and cation exchange resin may be used individually or in combination as, for example, in the case of a mixed resin bed having both anion and cation exchange resins.
To coagulate the obtained copolymer latex, any coagulant which is commonly used for coagulation of a fluoropolymer latex may be used, and it may, for example, be a water-soluble salt (e.g., calcium chloride, magnesium chloride, aluminum chloride or aluminum nitrate), an acid (e.g., nitric acid, hydrochloric acid or sulfuric acid), or a water-soluble organic liquid (e.g., alcohol or acetone). The amount of the coagulant to be added may be in a range of 0.001 to 20 parts by mass, for example, in a range of 0.01 to 10 parts by mass per 100 parts by mass of the latex. Alternatively or additionally, the latex may be frozen for coagulation or mechanically coagulated, for example, with a homogenizer as described in U.S. Pat. No. 5,463,021 (Beyer et al.). Alternatively or additionally, the latex may be coagulated by adding polycations. It may also be useful to avoid acids and alkaline earth metal salts as coagulants to avoid metal contaminants. To avoid coagulation altogether and any contaminants from coagulants, spray drying the latex after polymerization and optional ion-exchange purification may be useful to provide solid copolymer.
A coagulated copolymer can be collected by filtration and washed with water. The washing water may, for example, be ion-exchanged water, pure water, or ultrapure water. The amount of the washing water may be from 1 to 5 times by mass to the copolymer or ionomer, whereby the amount of the emulsifier attached to the copolymer can be sufficiently reduced by one washing.
The copolymer produced can have less than 50 ppm metal ion content, in some embodiments, less than 25 ppm, less than 10 ppm, less than 5 ppm, or less than 1 ppm metal ion content. Specifically, metal ions such as alkali metals, alkaline earth metal, heavy metals (e.g., nickel, cobalt, manganese, cadmium, and iron) can be reduced. To achieve a metal ion content of less than 50 ppm, 25 ppm, 10 ppm. 5 ppm, or 1 ppm, polymerization can be conducted in the absence of added metal ions. For example, potassium persulfate, a common alternative initiator or co-initiator with ammonium persulfate, is not used, and mechanical and freeze coagulation described above may be used instead of coagulation with metal salts. It is also possible to use organic initiators as disclosed in U.S. Pat. No. 5,182,342 (Feiring et al.). To achieve such low ion content, ion exchange can be used, as described above, and the water for polymerization and washing may be deionized.
The metal ion content of the copolymer can be measured by flame atomic absorption spectrometry after combusting the copolymer and dissolving the residue in an acidic aqueous solution.
For potassium as the analyte, the lower detection limit is less than 1 ppm.
In some embodiments of the methods of making the copolymer, radical polymerization also can be carried out by suspension polymerization. Suspension polymerization will typically produce particle sizes up to several millimeters.
A method for making the copolymer for the fluoropolymer dispersion disclosed herein can include copolymerizing components including SO2F-containing vinyl or allyl ethers (e.g., CF2═CF(CF2)a—O—CbF2b)c—O—(CeF2e)—SO2F), isolating a solid from the polymer dispersion, hydrolyzing the polymer, optionally purifying the polymer by ion exchange purification, and drying the resulting polymer. In some embodiments, the method of making the copolymer includes copolymerizing components including at least one compound represented by formula CF2═CF(CF2)a—(OCbF2b)c—O—(CeF2e)—SO3Z, optionally purifying the copolymer by ion-exchange purification, and spray drying the resulting dispersion. This method can conveniently eliminate the steps of isolating solid polymer and hydrolyzing, resulting in a more efficient and cost-effective process.
The components to be polymerized in the methods according to the present disclosure can include more than one compound represented by formula CF2═CF(CF2)a—(OCbF2b)c—O—(CeF2e)—SO3Z. When more than one compound represented by formula CF2═CF(CF2)a—(OCbF2b)c—O—(CeF2e)—SO3Z is present, each of a, b, c, e, and Z may be independently selected. In some of these embodiments, each Z is independently an alkali-metal cation or a quaternary ammonium cation.
In some cases, compounds represented by formula CF2═CF(CF2)a—(OCbF2b)—O—(CeF2e)—SO3Z are not prepared in situ from compounds represented by formula CF2═CF(CF2)a—(OCbF2b)c—O—(CeF2e)—SO2F. In some embodiments, the components to be polymerized in the method disclosed herein are substantially free of compounds represented by formula CF2═CF(CF2)a—(OCbF2b)c—O—(OCbF2b)c—O—(CeF2e)—SO2F. In this regard, “substantially free of compounds represented by formula CF2═CF(CF2)a—((OCbF2b)c—O—(CeF2e)—SO2F may mean that the components to be polymerized in the method disclosed herein are free of compounds represented by formula CF2═CF(CF2)a—(OCbF2b)c—O—(CeF2e)—SO2F or that such compounds are present in an amount of up to 5, 4, 3, 2, 1, 0.5, 0.1, 0.05, or 0.01 mole percent, based on the total amount of components.
In other embodiments, a copolymer of the present disclosure can be made by copolymerizing a compound represented by formula CF2═CF(CF2)a—(OCbF2b)c—O—(CeF2e)—SO2F and other fluorinated monomers as described above in any of their embodiments. In these embodiments, it is possible to hydrolyze some of the CF2═(CF(CF2)a—(OCbF2b)(c—O—(CeF2e)—SO2F (e.g., up to 5 ppm) to obtain an “in situ”-emulsifier as described above.
Fluoropolymers obtained by aqueous emulsion polymerization with inorganic initiators (e.g. persulfates, KMnO4, etc.) typically have a high number of unstable carbon-based end groups (e.g. more than 200 —COOM or —COF end groups per 106 carbon atoms, wherein M is hydrogen, a metal cation, or
NH2). For fluorinated ionomers useful, for example, in an electrochemical cell, the effect naturally increases as sulfonate equivalent weight decreases. These carbonyl end groups are vulnerable to peroxide radical attacks, which reduce the oxidative stability of the fluorinated ionomers. During operation of a fuel cell, electrolysis cell, or other electrochemical cell, peroxides can be formed. This degrades the fluorinated ionomers, and correspondingly reduces the operational life of the given electrolyte membrane.
As polymerized, the copolymer useful for the fluoropolymer dispersion according to the present disclosure can have up to 400 —COOM and —COF end groups per 106 carbon atoms, wherein M is independently an alkyl group, a hydrogen atom, a metallic cation, or a quaternary ammonium cation. Advantageously, in some embodiments, the copolymer according to the present disclosure has up to 200 unstable end groups per 106 carbon atoms. The unstable end groups are —COOM or —COF groups, wherein M is an alkyl group, a hydrogen atom, a metallic cation, or a quaternary ammonium cation. In some embodiments, the copolymer has up to 150, 100, 75, 50, 40, 30, 25, 20, 15, or 10 unstable end groups per 106 carbon atoms. The number of unstable end groups can be determined by Fourier-transform infrared spectroscopy using the method described below. In some embodiments, the copolymer according to the present disclosure has up to 50 (in some embodiments, up to 40, 30, 25, 20, 15, or 10) unstable end groups per 106 carbon atoms, as polymerized.
Copolymers useful for fluoropolymer dispersions according to some embodiments of the present disclosure have —SO2X″ end groups. As described above, —SO2X″ end groups can be introduced in the copolymers according to the present disclosure by generating SO3− radicals during the polymerization process. In some embodiments, reducing the number of unstable end groups can be accomplished by carrying out the polymerization in the methods disclosed above in the presence of a salt or pseudohalogen as described in U.S. Pat. No. 7,214,740 (Lochhaas et al.). Suitable salts can include a chloride anion, a bromide anion, an iodide anion, or a cyanide anion and a sodium, potassium, or ammonium cation. The salt used in the free-radical polymerization may be a homogenous salt or a blend of different salts. Examples of useful pseudohalogens are nitrile-containing compounds, which provide nitrile end groups.
Pseudohalogen nitrile-containing compounds have one or more nitrile groups and function in the same manner as compounds in which the nitrile groups are replaced with a halogen. Examples of suitable pseudohalogen nitrile-containing compounds include NC—CN, NC—S—S—CN, NCS—CN, Cl—CN, Br—CN, I—CN, NCN═NCN, and combinations thereof. During the free-radical polymerization, the reactive atoms/groups of the salts or the nitrile groups of the pseudohalogens chemically bond to at least one end of the backbone chain of the fluoropolymer. This provides CF2Y1 end groups instead of carbonyl end groups, wherein Y1 is chloro, bromo, iodo, or nitrile. For example, if the free-radical polymerization is performed in the presence of a KCl salt, at least one of the end groups provided would be a —CF2Cl end group. Alternatively, if the free-radical polymerization is performed in the presence of a NC—CN pseudohalogen, at least one of the end groups provided would be a —CF2CN end group.
Post-fluorination with fluorine gas can also be used to cope with unstable end groups and any concomitant degradation. Post-fluorination of the fluoropolymer can convert —COOH, amide, hydride, —COF, —CF2Y1 and other nonperfluorinated end groups or —CF═CF2 to —CF3 end groups. The post-fluorination may be carried out in any convenient manner. The post-fluorination can be conveniently C. and 250° C., in some embodiments in a range of 150° C. to 250° C. or 70° C. to 120° C., and pressures from 10 KPa to 1000 KPa. Reaction times can range from about four hours to about 16 hours. Under these conditions, most unstable carbon-based end groups are removed, whereas —SO2X groups mostly survive and are converted to —SO2F groups. In some embodiments, post-fluorination is not carried out when non-fluorinated monomers described above are used as monomers in the polymerization or when the copolymer according to the present disclosure includes divalent units independently represented by formula:
as described above in any of their embodiments.
The groups Y1 in the end groups —CF2Y1, described above, are reactive to fluorine gas, which reduces the time and energy required to post-fluorinate the copolymers in these embodiments. We have also found that the presence of alkali-metal cations in the copolymer increases the decomposition rate of unstable carboxylic end-groups and therefore makes a subsequent post-fluorination step, if needed, easier, faster, and cheaper.
Some conventional fluoropolymers can be difficult to disperse. A technique that can be useful for dispersing a fluoropolymer in a desired medium is up-concentration of a dilute dispersion of fluoropolymer. For example, U.S. Pat. Appl. Pub. Nos. 2017/0183435 (Ino) reports preparing a fluoropolymer electrolyte solution by heating a solid fluoropolymer electrolyte in a solution of 50% by weight solution of ethanol in water in an autoclave at 160° C. with stirring for five hours to achieve a fluoropolymer electrolyte solution with a solids concentration of 5% by weight. Concentration under reduced pressure provided a fluoropolymer electrolyte solution with a solids concentration of 20% by weight.
By contrast, the method of the present disclosure allows for direct dispersion of the copolymer disclosed herein at a concentration of at least 10, 15, 20, or 25 percent by weight in a solution of water and organic solvent without the need for up-concentrating. In some embodiments, the method of the present disclosure allows for direct dispersion of the copolymer disclosed herein at a concentration of up to 30, 40, or 50 percent by weight in a solution of water and organic solvent without the need for up-concentrating. For the method of the present disclosure, it should be understood that combining components comprising at least ten percent by weight of the copolymer, based on the total weight of the components, refers to the concentration of the copolymer when the components are initially combined (e.g., when organic solvent is first added to an aqueous dispersion of the fluoropolymer) before any agitation of the combined components. In some embodiments of the method of the present disclosure, Z is hydrogen. Examples of suitable organic solvents useful for preparing the fluoropolymer dispersions of the present disclosure include, lower alcohols (e.g., methanol, ethanol, isopropanol, n-propanol), polyols (e.g., ethylene glycol, propylene glycol, glycerol), ethers (e.g., tetrahydrofuran and dioxane), diglyme, polyglycol ethers, ether acetates, acetonitrile, acetone, dimethylsulfoxide (DMSO), N,N dimethyacetamide (DMA), ethylene carbonate, propylene carbonate, dimethylcarbonate, diethylcarbonate, N,N-dimethylformamide (DMF), N-methylpyrrolidinone (NMP), dimethylimidazolidinone, butyrolactone, hexamethylphosphoric triamide (HMPT), isobutyl methyl ketone, sulfolane, and combinations thereof. In some embodiments, the copolymer, water, and organic solvent can be heated at a pressure of up to 0.2 MPa or 0.15 MPa at a temperature of up to 100° C., 90° C., 80° C., 70° C., 60° C., 50° C., or 40° C. Advantageously, the fluoropolymer dispersion may also be made at ambient temperature and pressure. Also advantageously, the fluoropolymer dispersions according to the present disclosure have useful viscosities even with a high concentration of copolymer.
The fluoropolymer dispersion of the present disclosure may be useful, for example, in the manufacture of catalyst ink and polymer electrolyte membranes for use in fuel cells or other electrolytic cells. A membrane electrode assembly (MEA) is the central element of a proton exchange membrane fuel cell, such as a hydrogen fuel cell. Fuel cells are electrochemical cells which produce usable electricity by the catalyzed combination of a fuel such as hydrogen and an 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 electrolyte. One face of the PEM is in contact with an anode electrode layer and the opposite face is in contact with a cathode electrode layer. Each electrode layer includes electrochemical catalysts, typically including platinum metal. Gas diffusion layers (GDL's) facilitate gas transport to and from the anode and cathode electrode materials and 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 may be applied to GDL's in the form of a catalyst ink, and the resulting coated GDL's sandwiched with a PEM to form a five-layer MEA. Alternately, the anode and cathode electrode layers may be applied to opposite sides of the PEM in the form of a catalyst ink, and the resulting catalyst-coated membrane (CCM) sandwiched with two GDL's to form a five-layer MEA. Details concerning the preparation of catalyst inks and their use in membrane assemblies can be found, for example, in U.S. Pat. Publ. No. 2004/0107869 (Velamakanni et al.). In atypical PEM fuel cell, protons are formed at the anode via hydrogen oxidation and transported across the PEM to the cathode to react with oxygen, causing electrical current to flow in an external circuit connecting the electrodes. The PEM forms a durable, non-porous, electrically non-conductive mechanical barrier between the reactant gases, yet it also passes H1+ ions readily.
The fluoropolymer dispersion of the present disclosure may be useful as and/or useful for making a catalyst ink composition. In some embodiments, the fluoropolymer dispersion further comprises catalyst particles (e.g., metal particles or carbon-supported metal particles). A variety of catalysts may be useful. Typically, carbon-supported catalyst particles are used. Typical carbon-supported catalyst particles are 50% to 90% carbon and 10% to 50% catalyst metal by weight, the catalyst metal typically comprising platinum for the cathode and platinum and ruthenium in a weight ratio of 2:1 for the anode.
However, other metals may be useful, for example, gold, silver, palladium, iridium, rhodium, ruthenium, iron, cobalt, nickel, chromium, tungsten, manganese, vanadium, and alloys thereof. To make an MEA or CCM, catalyst may be applied to the PEM by any suitable means, including both hand and machine methods, including hand brushing, notch bar coating, fluid bearing die coating, wire-wound rod coating, fluid bearing coating, slot-fed knife coating, three-roll coating, or decal transfer. Coating may be achieved in one application or in multiple applications. Advantageously, fluoropolymer dispersions according to the present disclosure may be useful for making a catalyst layer with one coating application. The catalyst ink may be applied to a PEM or a GDL directly, or the catalyst ink may be applied to a transfer substrate, dried, and thereafter applied to the PEM or to the FTL as a decal.
In some embodiment, the catalyst ink includes the copolymer disclosed herein at a concentration of at least 10, 15, or 20 percent by weight and up to 30 percent by weight, based on the total weight of the catalyst ink. In some embodiment, the catalyst ink includes the catalyst particles in an amount of at least 10, 15, or 20 percent by weight and up to 50, 40, or 30 percent by weight, based on the total weight of the catalyst ink. The catalyst particles may be added to the fluoropolymer dispersion made as described above in any of its embodiments. The resulting catalyst ink may be mixed, for example, with heating.
The percent solid in the catalyst ink may be selected, for example, to obtain desirable rheological properties. Examples of suitable organic solvents useful for including in the catalyst ink include, lower alcohols (e.g., methanol, ethanol, isopropanol, n-propanol), polyols (e.g., ethylene glycol, propylene glycol, glycerol), ethers (e.g., tetrahydrofuran and dioxane), diglyme, polyglycol ethers, ether acetates, acetonitrile, acetone, dimethylsulfoxide (DMSO), N,N dimethyacetamide (DMA), ethylene carbonate, propylene carbonate, dimethylcarbonate, diethylcarbonate, N,N-dimethylformamide (DMF), N-methylpyrrolidinone (NMP), dimethylimidazolidinone, butyrolactone, hexamethylphosphoric triamide (HMPT), isobutyl methyl ketone, sulfolane, and combinations thereof. In some embodiments, the catalyst ink contains 0% to 50% by weight of a lower alcohol and 0% to 20% by weight of a polyol. In addition, the ink may contain 0% to 2% of a suitable dispersant.
In some embodiments, the fluoropolymer dispersion may be useful for making a polymer electrolyte membrane. The fluoropolymer dispersion may be formed into a polymer electrolyte membrane by any suitable method, including casting, molding, and extrusion. Typically, the membrane is cast from the fluoropolymer dispersion and then dried, annealed, or both. The copolymer may be cast from a suspension. Any suitable casting method may be used, including bar coating, spray coating, slit coating, and brush coating. After forming, the membrane may be annealed, typically at a temperature of 120° C. or higher, more typically 130° C. or higher, most typically 150° C. or higher. In some embodiments of the method according to the present disclosure, a polymer electrolyte membrane can be obtained by obtaining the fluoropolymer dispersion, optionally purifying the dispersion by ion-exchange purification, and concentrating the dispersion to make a membrane. Typically, if the fluoropolymer dispersion is to be used to form a membrane, the concentration of copolymer is advantageously high (e.g., at least 20, 30, or 40 percent by weight). Often a water-miscible organic solvent is added to facilitate film formation. Examples of water-miscible solvents include, lower alcohols (e.g., methanol, ethanol, isopropanol, n-propanol), polyols (e.g., ethylene glycol, propylene glycol, glycerol), ethers (e.g., tetrahydrofuran and dioxane), ether acetates, acetonitrile, acetone, dimethylsulfoxide (DMSO), N,N dimethyacetamide (DMA), ethylene carbonate, propylene carbonate, dimethylcarbonate, diethylcarbonate, N,N-dimethylformamide (DMF), N-methylpyrrolidinone (NMP), dimethylimidazolidinone, butyrolactone, hexamethylphosphoric triamide (HMPT), isobutyl methyl ketone, sulfolane, and combinations thereof.
The present disclosure provides a membrane electrode assembly comprising at least one of a catalyst ink comprising and/or prepared from the fluoropolymer dispersion of the present disclosure or a polymer electrolyte membrane made from the fluoropolymer dispersion of the present disclosure. In some embodiments, the polymer electrolyte membrane and catalyst ink use embodiments of the copolymer disclosed herein. The catalyst ink and polymer electrolyte membrane may use the same or different copolymers. In some embodiments, the catalyst ink comprises and/or is prepared from the fluoropolymer dispersion of the present disclosure, and the polymer electrolyte membrane includes a conventional copolymer (e.g., one that does not include one or more divalent units independently represented by formula:
In some embodiments, the polymer electrolyte membrane is prepared from the fluoropolymer dispersion of the present disclosure, and the catalyst ink includes a conventional copolymer (e.g., one that does not include one or more divalent units independently represented by formula:
In some embodiments of the fluoropolymer dispersion of the present disclosure, a salt of at least one of cerium, manganese or ruthenium or one or more cerium oxide or zirconium oxide compounds is added to the acid form of the copolymer before membrane formation. Typically the salt of cerium, manganese, or ruthenium and/or the cerium or zirconium oxide compound is mixed well with or dissolved within the copolymer to achieve substantially uniform distribution.
The salt of cerium, manganese, or ruthenium may comprise any suitable anion, including chloride, bromide, hydroxide, nitrate, sulfonate, acetate, phosphate, and carbonate. More than one anion may be present. Other salts may be present, including salts that include other metal cations or ammonium cations. Once cation exchange occurs between the transition metal salt and the acid form of the ionomer, it may be desirable for the acid formed by combination of the liberated proton and the original salt anion to be removed. Thus, it may be useful to use anions that generate volatile or soluble acids, for example chloride or nitrate. Manganese cations may be in any suitable oxidation state, including Mn2+, Mn3+, and Me, but are most typically Mn2+. Ruthenium cations may be in any suitable oxidation state, including Ru3+and Re, but are most typically Ru3+. Cerium cations may be in any suitable oxidation state, including Ce3+ and Ce4+. Without wishing to be bound by theory, it is believed that the cerium, manganese, or ruthenium cations persist in the polymer electrolyte because they are exchanged with H+ ions from the anion groups of the polymer electrolyte and become associated with those anion groups. Furthermore, it is believed that polyvalent cerium, manganese, or ruthenium cations may form crosslinks between anion groups of the polymer electrolyte, further adding to the stability of the polymer. In some embodiments, the salt may be present in solid form. The cations may be present in a combination of two or more forms including solvated cation, cation associated with bound anion groups of the polymer electrolyte membrane, and cation bound in a salt precipitate. The amount of salt added is typically between 0.001 and 0.5 charge equivalents based on the molar amount of acid functional groups present in the polymer electrolyte, more typically between 0.005 and 0.2, more typically between 0.01 and 0.1, and more typically between 0.02 and 0.05. Further details for combining an anionic copolymer with cerium, manganese, or ruthenium cations can be found in U.S. Pat. Nos. 7,575,534 and 8,628,871, each to Frey et al.
The cerium oxide compound may contain cerium in the (IV) oxidation state, the (III) oxidation state, or both and may be crystalline or amorphous. The cerium oxide may be, for example, CeO2 or Ce2O3. The cerium oxide may be substantially free of metallic cerium or may contain metallic cerium. The cerium oxide may be, for example, a thin oxidation reaction product on a metallic cerium particle. The cerium oxide compound may or may not contain other metal elements. Examples of mixed metal oxide compounds comprising cerium oxide include solid solutions such as zirconia-ceria and multicomponent oxide compounds such as barium cerate. Without wishing to be bound by theory, it is believed that the cerium oxide may strengthen the polymer by chelating and forming crosslinks between bound anionic groups. The amount of cerium oxide compound added is typically between 0.01 and 5 weight percent based on the total weight of the copolymer, more typically between 0.1 and 2 weight percent, and more typically between 0.2 and 0.3 weight percent. The cerium oxide compound is typically present in an amount of less than 1% by volume relative to the total volume of the polymer electrolyte membrane, more typically less than 0.8% by volume, and more typically less than 0.5% by volume. Cerium oxide may be in particles of any suitable size, in some embodiments, between 1 nm and 5000 nm, 200 nm to 5000 nm, or 500 nm to 1000 nm. Further details regarding polymer electrolyte membranes including cerium oxide compounds can be found in U.S. Pat. No. 8,367,267 (Frey et al.).
The polymer electrolyte membrane, in some embodiments, may have a thickness of up to 90 microns, up to 60 microns, or up to 30 microns. A thinner membrane may provide less resistance to the passage of ions. In fuel cell use, this results in cooler operation and greater output of usable energy. Thinner membranes must be made of materials that maintain their structural integrity in use.
In some embodiments, the fluoropolymer dispersion of the present disclosure may be imbibed into a porous supporting matrix, typically in the form of a thin membrane having a thickness of up to 90 microns, up to 60 microns, or up to 30 microns. Any suitable method of imbibing the polymer into the pores of the supporting matrix may be used, including overpressure, vacuum, wicking, and immersion. In some embodiments, the copolymer is embedded in the matrix upon crosslinking. Any suitable supporting matrix may be used. Typically the supporting matrix is electrically non-conductive. Typically, the supporting matrix is composed of a fluoropolymer, which is more typically perfluorinated. Typical matrices include porous polytetrafluoroethylene (PTFE), such as biaxially stretched PTFE webs. In another embodiment fillers (e.g. fibers) might be added to the polymer to reinforce the membrane.
To make an MEA, GDL's may be applied to either side of a CCM by any suitable means. Any suitable GDL may be used in the practice of the present disclosure. Typically the GDL is comprised of sheet material comprising carbon fibers. Typically the GDL is a carbon fiber construction selected from woven and non-woven carbon fiber constructions. Carbon fiber constructions which may be useful in the practice of the present disclosure may include Toray™ Carbon Paper, SpectraCarb™ Carbon Paper, AFN™ non-woven carbon cloth, and Zoltek™ Carbon Cloth. The GDL may be coated or impregnated with various materials, including carbon particle coatings, hydrophilizing treatments, and hydrophobizing treatments such as coating with polytetrafluoroethylene (PTFE).
In use, the MEA according to the present disclosure is typically sandwiched between two rigid plates, known as distribution plates, also known as bipolar plates (BPP's) or monopolar plates. Like the GDL, the distribution plate is typically electrically conductive. The distribution plate is typically made of a carbon composite, metal, or plated metal material. The distribution plate distributes reactant or product fluids to and from the MEA electrode surfaces, typically through one or more fluid-conducting channels engraved, milled, molded or stamped in the surface(s) facing the MEA(s). These channels are sometimes designated a flow field. The distribution plate may distribute fluids to and from two consecutive MEA's in a stack, with one face directing fuel to the anode of the first MEA while the other face directs oxidant to the cathode of the next MEA (and removes product water), hence the term “bipolar plate.” Alternately, the distribution plate may have channels on one side only, to distribute fluids to or from an MEA on only that side, which may be termed a “monopolar plate.” A typical fuel cell stack comprises a number of MEA's stacked alternately with bipolar plates.
Another type of electrochemical device is an electrolysis cell, which uses electricity to produce chemical changes or chemical energy. An example of an electrolysis cell is a chlor-alkali membrane cell where aqueous sodium chloride is electrolyzed by an electric current between an anode and a cathode.
The electrolyte is separated into an anolyte portion and a catholyte portion by a membrane subject to harsh conditions. In chlor-alkali membrane cells, caustic sodium hydroxide collects in the catholyte portion, hydrogen gas is evolved at the cathode portion, and chlorine gas is evolved from the sodium chloride-rich anolyte portion at the anode. The fluoropolymer dispersion of the present disclosure may be useful, for example, in the manufacture of catalyst ink and electrolyte membranes for use in chlor-alkali membrane cells or other electrolytic cells.
The copolymer according to the present disclosure may also be useful has a binder for an electrode in other electrochemical cells (for example, lithium ion batteries). To make electrodes, powdered active ingredients can be dispersed in a solvent with the copolymer and coated onto a metal foil substrate, or current collector. The resulting composite electrode contains the powdered active ingredient in the polymer binder adhered to the metal substrate. Useful active materials for making negative electrodes include alloys of main group elements and conductive powders such as graphite. Examples of useful active materials for making a negative electrode include oxides (tin oxide), carbon compounds (e.g., artificial graphite, natural graphite, soil black lead, expanded graphite, and scaly graphite), silicon carbide compounds, silicon-oxide compounds, titanium sulfides, and boron carbide compounds. Useful active materials for making positive electrodes include lithium compounds, such as Li4/3Ti5/3O4, LiV3O8, LiV2O5, LiCo0.2Ni0.8O2, LiNiO2, LiFePO4, LiMnPO4, LiCoPO4, LiMn2O4, and LiCoO2. The electrodes can also include electrically conductive diluents and adhesion promoters.
Electrochemical cells including the copolymer disclosed herein as a binder can be made by placing at least one each of a positive electrode and a negative electrode in an electrolyte. Typically, a microporous separator can be used to prevent the contact of the negative electrode directly with the positive electrode. Once the electrodes are connected externally, lithiation and delithiation can take place at the electrodes, generating a current. A variety of electrolytes can be employed in a lithium-ion cell. Representative electrolytes contain one or more lithium salts and a charge-carrying medium in the form of a solid, liquid, or gel. Examples of lithium salts include LiPF6, LiBF4, LiClO4, lithium bis(oxalato)borate, LiN(CF3SO2)2, LiN(C2F5SO2)2, LiAsF6, LiC(CF3SO2)3, and combinations thereof Examples of solid charge carrying media include polymeric media such as polyethylene oxide, polytetrafluoroethylene, polyvinylidene fluoride, fluorine-containing copolymers, polyacrylonitrile, combinations thereof, and other solid media that will be familiar to those skilled in the art. Examples of liquid charge carrying media include ethylene carbonate, propylene carbonate, dimethyl carbonate, diethyl carbonate, ethyl methyl carbonate, butylene carbonate, vinylene carbonate, fluoroethylene carbonate, fluoropropylene carbonate, gamma-butyrolactone, methyl difluoroacetate, ethyl difluoroacetate, dimethoxyethane, diglyme (bis(2-methoxyethyl) ether), tetrahydrofuran, dioxolane, combinations thereof and other media that will be familiar to those skilled in the art. Examples of charge carrying media gels include those described in U.S. Pat. No. 6,387,570 (Nakamura et al.) and U.S. Pat. No. 6,780,544 (Noh). The electrolyte can include other additives (e.g., a cosolvent or a redox chemical shuttle).
The electrochemical cells can be useful as rechargeable batteries and can be used in a variety of devices, including portable computers, tablet displays, personal digital assistants, mobile telephones, motorized devices (e.g., personal or household appliances and vehicles), instruments, illumination devices (e.g., flashlights) and heating devices. One or more of the electrochemical cells can be combined to provide battery pack.
In a first embodiment, the present disclosure provides fluoropolymer dispersion comprising water and a copolymer comprising:
wherein a is 0 or 1, b is 2 to 8, c is 0 to 2, e is 1 to 8 with the proviso that when a and c are 0, then e is 3 to 8, and Z is independently a hydrogen, alkyl having up to four carbon atoms, an alkali-metal cation, or a quaternary ammonium cation; and
one or more divalent units independently represented by formula:
wherein Rf is a linear or branched perfluoroalkyl group having from 1 to 8 carbon atoms and optionally interrupted by one or more —O—groups, z is 0, 1, or 2, each n is independently 1, 2, 3, or 4, and m is 0 or 1;
wherein the fluoropolymer dispersion comprises at least 10% by weight of the copolymer, based on the total weight of the dispersion, wherein the copolymer has an —SO3Z equivalent weight in a range from 600 to 2000, and wherein a variation of the copolymer in which —SO3Z is replaced with —SO2F has a melt flow index of up to 80 grams per ten minutes measured at a temperature of 265° C. and at a support weight of 5 kg.
In a second embodiment, the present disclosure provides the fluoropolymer dispersion of the first embodiment, wherein b is 2 or 3, c is 0 or 1, and e is 4.
In a third embodiment, the present disclosure provides the fluoropolymer dispersion of the first embodiment, wherein b is 2 or 3, c is 1, and e is 2 or 4.
In a fourth embodiment, the present disclosure provides the fluoropolymer dispersion of any one of the first to third embodiments, wherein when a is 0, then n is not 3.
In a fifth embodiment, the present disclosure provides the fluoropolymer dispersion of any one of the first to fourth embodiments, wherein z is 1 or 2, CnF2n is (CF2)n, and n is 1, 2, or 3.
In a sixth embodiment, the present disclosure provides the fluoropolymer dispersion of any one of the first to fifth embodiments, wherein at least one n is 1.
In a seventh embodiment, the present disclosure provides the fluoropolymer dispersion of any one of the first to sixth embodiments, wherein the copolymer further comprises at least one of divalent units derived from chlorotrifluoroethylene or divalent units derived from hexafluoropropylene.
In an eighth embodiment, the present disclosure provides the fluoropolymer dispersion of any one of the first to seventh embodiments, wherein the copolymer has an alpha transition temperature [T(α)] of at least 100° C.
In a ninth embodiment, the present disclosure provides the fluoropolymer dispersion of any one of the first to seventh embodiments, wherein the copolymer has a T(α) of up to 100° C. or less than 100° C.
In a tenth embodiment, the present disclosure provides the fluoropolymer dispersion of any one of the first to ninth embodiments, wherein the copolymer further comprises divalent units independently represented by formula:
wherein p is 0 or 1, q is 2 to 8, r is 0 to 2, s is 1 to 8, and Z′ is a hydrogen, an alkyl group having up to four carbon atoms, an alkali-metal cation or a quaternary ammonium cation.
In an eleventh embodiment, the present disclosure provides the fluoropolymer dispersion of any one of the first to tenth embodiments, wherein the divalent units comprise at least 60 mole % of —[CF2—CF2]—, based on the total amount of divalent units in the copolymer.
In a twelfth embodiment, the present disclosure provides the fluorinated dispersion of any one of the first to eleventh embodiments, wherein the divalent units represented by formula
are present at up to 20 or up to 15 mole percent, or in a range from 3 to 20 or 4 to 15 mole percent, based on the total moles of divalent units in the copolymer.
In a thirteenth embodiment, the present disclosure provides the fluorinated dispersion of any one of the first to twelfth embodiments, wherein the divalent units represented by formula
are present at up to 30 or up to 25 mole percent, or in a range from 10 to 30 or 15 to 25 mole percent, based on the total moles of divalent units in the copolymer.
In a fourteenth embodiment, the present disclosure provides the fluoropolymer dispersion of any one of the first to thirteenth embodiments, wherein the copolymer further comprises divalent units are derived from bisolefins represented by formula X2C═CY—(CW2)m—(O)n—RF—(O)o—(CW2)p—CY=CX2, wherein each of X, Y, and W is independently fluoro, hydrogen, alkyl, alkoxy, polyoxyalkyl, perfluoroalkyl, perfluoroalkoxy or perfluoropolyoxyalkyl, m and p are independently an integer from 0 to 15, and n, o are independently 0 or 1.
In a fifteenth embodiment, the present disclosure provides the fluoropolymer dispersion of the fourteenth embodiment, wherein X, Y, and W are each independently fluoro, CF3, C2F5, C3F7, C4F9, hydrogen, CH3, C2H5, C3H7, C4H9. In a sixteenth embodiment, the present disclosure provides the fluoropolymer dispersion of any one of the first to fifteenth embodiments, wherein Z is an alkali metal cation.
In a seventeenth embodiment, the present disclosure provides the fluoropolymer dispersion of the sixteenth embodiment, wherein Z is sodium.
In an eighteenth embodiment, the present disclosure provides the fluoropolymer dispersion of any one of the first to fifteenth embodiments, wherein Z is hydrogen.
In a nineteenth embodiment, the present disclosure provides the fluoropolymer dispersion of any one of the first to eighteenth embodiments, wherein the copolymer has an —SO2X equivalent weight greater than 1000.
In a twentieth embodiment, the present disclosure provides the fluoropolymer dispersion of any one of the first to nineteenth embodiments, wherein the copolymer further comprises divalent units derived from at least one of ethylene, propylene, isobutylene, ethyl vinyl ether, vinyl benzoate, ethyl allyl ether, cyclohexyl allyl ether, norbornadiene, crotonic acid, an alkyl crotonate, acrylic acid, an alkyl acrylate, methacrylic acid, an alkyl methacrylate, or hydroxybutyl vinyl ether.
In a twenty-first embodiment, the present disclosure provides the fluoropolymer dispersion of any one of the first to twentieth embodiments, wherein the copolymer has up to 100 —COOM and —COF end groups per 106 carbon atoms, wherein M is independently an alkyl group, a hydrogen atom, a metallic cation, or a quaternary ammonium cation.
In a twenty-second embodiment, the present disclosure provides the fluoropolymer dispersion of any one of the first to twenty-first embodiments. wherein the copolymer comprises less than 25 ppm metal ions.
In a twenty-third embodiment, the present disclosure provides the fluoropolymer dispersion of any one of the first to twenty-second embodiments, wherein the copolymer comprises —SO2X end groups.
In a twenty-fourth embodiment, the present disclosure provides the fluoropolymer dispersion of any one of the first to twenty-third embodiments, wherein the fluoropolymer dispersion comprises at least 15% by weight of the copolymer, based on the total weight of the dispersion.
In a twenty-fifth embodiment, the present disclosure provides the fluoropolymer dispersion of any one of the first to twenty-fourth embodiments, wherein the fluoropolymer dispersion comprises at least 25% by weight of the copolymer, based on the total weight of the dispersion.
In a twenty-sixth embodiment, the present disclosure provides the fluoropolymer dispersion of any one of the first to twenty-fifth embodiments, wherein the variation of the copolymer in which —SO3Z is replaced with —SO2F has a melt flow index of up to 40 grams per ten minutes measured at a temperature of 265° C. and at a support weight of 5 kg.
In a twenty-seventh embodiment, the present disclosure provides the fluoropolymer dispersion of any one of the first to twenty-sixth embodiments, wherein the variation of the copolymer in which —SO3Z is replaced with -SO2F has a melt flow index of up to 25 grams per ten minutes measured at a temperature of 265° C. and at a support weight of 5 kg.
In a twenty-eighth embodiment, the present disclosure provides the fluoropolymer dispersion of any one of the first to twenty-seventh embodiments, wherein the variation of the copolymer in which SO3Z is replaced with —SO2F has a glass transition temperature of up to 20° C. In a twenty-ninth embodiment, the present disclosure provides the fluoropolymer dispersion of any one of the first to twenty-eighth embodiments, further comprising organic solvent
In a thirtieth embodiment, the present disclosure provides the fluoropolymer dispersion of any one of the first to twenty-ninth embodiments, further comprising catalyst particles.
In a thirty-first embodiment, the present disclosure provides a catalyst ink comprising the fluoropolymer dispersion of any one of the first to thirtieth embodiments. In a thirty-second embodiment, the present disclosure provides a polymer electrolyte membrane prepared from the fluoropolymer dispersion of any one of the first to twenty-ninth embodiments.
In a thirty-third embodiment, the present disclosure provides the polymer electrolyte membrane of the twenty-fifth embodiment, wherein the polymer electrolyte membrane further comprises at least one of cerium cations, manganese cations, ruthenium cations, or a cerium oxide. In a thirty-fourth embodiment, the present disclosure provides the polymer electrolyte membrane of the thirty-third embodiment, wherein the at least one of cerium cations, manganese cations, or ruthenium cations are present in a range from 0.2 to 20 percent relative to the amount of sulfonate groups in the copolymer.
In a thirty-fifth embodiment, the present disclosure provides a membrane electrode assembly comprising at least one of the polymer electrolyte membrane of any one of the thirty-second to thirty-fourth embodiments or the catalyst ink of the thirty-first embodiment.
In a thirty-sixth embodiment, the present disclosure provides a binder for an electrode comprising the fluoropolymer dispersion of any one of the first to twenty-ninth embodiments.
In a thirty-seventh embodiment, the present disclosure provides an electrochemical cell comprising the binder of the thirty-sixth embodiment.
In a thirty-eighth embodiment, the present disclosure provides a method of making a fluoropolymer dispersion, the method comprising:
combining components comprising water, an organic solvent, and at least ten percent by weight of a copolymer, based on the total weight of the components, the copolymer comprising:
In a thirty-ninth embodiment, the present disclosure provides the method of the thirty-eighth embodiment, further comprising forming the fluoropolymer dispersion into a film.
In a fortieth embodiment, the present disclosure provides the method of the thirty-eighth or thirty-ninth embodiment, wherein when a and c are 0, then e is 3 to 8.
In a forty-first embodiment, the present disclosure provides the method of any one of the thirty-eighth to fortieth embodiments, wherein b is 2 or 3, c is 0 or 1, and e is 4.
In a forty-second embodiment, the present disclosure provides the method of any one of the thirty-eighth to forty-first embodiments, b is 2 or 3, c is 1, and e is 2 or 4.
In a forty-third embodiment, the present disclosure provides the method of any one of the thirty-eighth to forty-second embodiments, wherein the copolymer comprises anionic species that are not covalently bound to the ionomer, the method further comprising contacting the fluoropolymer dispersions with an anion exchange resin having associated hydroxide ions, and exchanging at least a portion of the anionic species with the hydroxide ions to provide an anionic exchanged dispersion.
In a forty-fourth embodiment, the present disclosure provides the method of any one of the thirty-eighth to forty-third embodiments, wherein the copolymer comprises cationic species that are not covalently bound to the copolymer, the method further comprising contacting fluoropolymer dispersion with a cation exchange resin having acidic protons, and exchanging at least a portion of the cationic species with the protons to provide cation-exchanged dispersion.
In a forty-fifth embodiment, the present disclosure provides the method of any one of the thirty-eighth to forty-fourth embodiments, further comprising spray drying the copolymer.
In a forty-sixth embodiment, the present disclosure provides the method of any one of the thirty-eighth to forty-fifth embodiments, further comprising post-fluorinating the copolymer.
In a forty-seventh embodiment, the present disclosure provides the method of any one of the thirty-eighth to forty-sixth embodiments, wherein when a is 0, then n is not 3.
In a forty-eighth embodiment, the present disclosure provides the method of any one of the thirty-eighth to forty-seventh embodiments, wherein z is 1 or 2, CnF2n is (CF2)n, and n is 1, 2, or 3.
In a forty-ninth embodiment, the present disclosure provides the method of any one of the thirty-eighth to forty-eighth embodiments, wherein at least one n is 1.
In a fiftieth embodiment, the present disclosure provides the method of any one of the thirty-eighth to forty-ninth embodiments, wherein the copolymer further comprises at least one of divalent units derived from chlorotrifluoroethylene or divalent units derived from hexafluoropropylene.
In a fifty-first embodiment, the present disclosure provides the method of any one of the thirty-eighth to fiftieth embodiments, wherein the copolymer has an alpha transition temperature [T(α)] of at least 100° C.
In a fifty-second embodiment, the present disclosure provides the method of any one of the thirty-eighth to fiftieth embodiments, wherein the copolymer has an alpha transition temperature [T(α)] of up to 100° C. or less than 100° C.
In a fifty-third embodiment, the present disclosure provides the method of any one of the thirty-eighth to fifty-second embodiments, wherein the copolymer further comprises divalent units independently represented by formula:
wherein p is 0 or 1, q is 2 to 8, r is 0 to 2, s is 1 to 8, and Z′ is a hydrogen, an alkyl group having up to four carbon atoms, an alkali-metal cation or a quaternary ammonium cation.
In a fifty-fourth embodiment, the present disclosure provides the method of any one of the thirty-eighth to fifty-third embodiments, wherein the divalent units comprise at least 60 mole % of —[CF2—CF2]—, based on the total amount of divalent units in the copolymer.
In a fifty-fifth embodiment, the present disclosure provides the method of any one of the thirty-eighth to fifty-fourth embodiments, wherein the divalent units represented by formula
are present at up to 20 or up to 15 mole percent, or in a range from 3 to 20 or 4 to 15 mole percent, based on the total moles of divalent units in the copolymer.
In a fifty-sixth embodiment, the present disclosure provides the method of any one of the thirty-eighth to fifty-fifth embodiments, wherein the divalent units represented by formula
are present at up to 30 or up to 25 mole percent, or in a range from 10 to 30 or 15 to 25 mole percent, based on the total moles of divalent units in the copolymer.
In a fifty-seventh embodiment, the present disclosure provides the method of any one of the thirty-eighth to fifty-sixth embodiments, wherein the copolymer further comprises divalent units that are derived from bisolefins represented by formula X2C═CY—(CW2)m—(O)n—RF—(O)o—(CW2)p—CY═CX2, wherein each of X, Y, and W is independently fluoro, hydrogen, alkyl, alkoxy, polyoxyalkyl, perfluoroalkyl, perfluoroalkoxy or perfluoropolyoxyalkyl, m and p are independently an integer from 0 to 15, and n, o are independently 0 or 1.
In a fifty-eighth embodiment, the present disclosure provides the method of the fifty-seventh embodiment, wherein X, Y, and W are each independently fluoro, CF3, C2F5, C3F7, C4F9, hydrogen, CH3, C2H5, C3H7, C4H9.
In a fifty-ninth embodiment, the present disclosure provides the method of any one of the thirty-eighth to fifty-eighth embodiments, wherein Z is an alkali metal cation.
In a sixtieth embodiment, the present disclosure provides the method of the fifty-ninth embodiment, wherein Z is sodium.
In a sixty-first embodiment, the present disclosure provides the method of any one of the thirty-eighth to fifty-eighth embodiments, wherein Z is hydrogen.
In a sixty-second embodiment, the present disclosure provides the method of any one of the thirty-eighth to sixty-first embodiments, wherein the copolymer has an —SO2X equivalent weight greater than 1000.
In a sixty-third embodiment, the present disclosure provides the method of any one of the thirty-eighth to sixty-second embodiments, wherein the copolymer further comprises divalent units derived from at least one of ethylene, propylene, isobutylene, ethyl vinyl ether, vinyl benzoate, ethyl allyl ether, cyclohexyl allyl ether, norbornadiene, crotonic acid, an alkyl crotonate, acrylic acid, an alkyl acrylate, methacrylic acid, an alkyl methacrylate, or hydroxybutyl vinyl ether.
In a sixty-fourth embodiment, the present disclosure provides the method of any one of the thirty-eighth to sixty-third embodiments, wherein the copolymer has up to 100 —COOM and —COF end groups per 106 carbon atoms, wherein M is independently an alkyl group, a hydrogen atom, a metallic cation, or a quaternary ammonium cation.
In a sixty-fifth embodiment, the present disclosure provides the method of any one of the thirty-eighth to sixty-fourth embodiments. wherein the copolymer comprises less than 25 ppm metal ions.
In a sixty-sixth embodiment, the present disclosure provides the method of any one of the thirty-eighth to sixty-fifth embodiments, wherein the copolymer comprises —SO2X end groups.
In a sixty-seventh embodiment, the present disclosure provides the method of any one of the thirty-eighth to sixty-sixth embodiments, wherein the fluoropolymer dispersion comprises at least 20% by weight of the copolymer, based on the total weight of the dispersion.
In a sixty-eighth embodiment, the present disclosure provides the method of any one of the thirty-eighth to sixty-seventh embodiments, wherein the fluoropolymer dispersion comprises at least 25% by weight of the copolymer, based on the total weight of the dispersion.
In a sixty-ninth embodiment, the present disclosure provides the method of any one of the thirty-eighth to sixty-eighth embodiments, wherein a variation of the copolymer in which —SO3Z is replaced with —SO2F has a melt flow index of up to 80 grams per ten minutes measured at a temperature of 265° C. and at a support weight of 5 kg.
In a seventieth embodiment, the present disclosure provides the method of any one of the thirty-eighth to sixty-ninth embodiments, wherein a variation of the copolymer in which —SO3Z is replaced with —SO2F has a melt flow index of up to 40 grams per ten minutes measured at a temperature of 265° C. and at a support weight of 5 kg.
In a seventy-first embodiment, the present disclosure provides the method of any one of the thirty-eighth to seventieth embodiments, wherein the variation of the copolymer in which SO3Z is replaced with —SO2F has a glass transition temperature of up to 25° C. or up to 20° C.
In a seventy-second embodiment, the present disclosure provides the method of any one of the thirty-eighth to seventy-first embodiments, wherein the fluoropolymer dispersion further comprises catalyst particles.
In a seventy-third embodiment, the present disclosure provides a catalyst ink made by the method of any one of the thirty-eighth to seventy-second embodiments.
In a seventy-fourth embodiment, the present disclosure provides a polymer electrolyte membrane prepared from the method of any one of the thirty-eighth to seventy-third embodiments.
In a seventy-fifth embodiment, the present disclosure provides the polymer electrolyte membrane of the seventy-fourth embodiment, wherein the polymer electrolyte membrane further comprises at least one of cerium cations, manganese cations, ruthenium cations, or a cerium oxide.
In a seventy-sixth embodiment, the present disclosure provides the polymer electrolyte membrane of the seventy-fifth embodiment, wherein the at least one of cerium cations, manganese cations, or ruthenium cations are present in a range from 0.2 to 20 percent relative to the amount of sulfonate groups in the copolymer.
In a seventy-seventh embodiment, the present disclosure provides a membrane electrode assembly comprising at least one of the polymer electrolyte membrane made by the method of any one of the seventy-fourth to seventy-sixth embodiments or the catalyst ink made by the method of the seventy-third embodiment.
In a seventy-eighth embodiment, the present disclosure provides a binder for an electrode made by the method of any one of the thirty-eighth to seventy-third embodiments.
In a seventy-ninth embodiment, the present disclosure provides an electrochemical cell comprising the binder of the seventy-eighth embodiment.
In order that this disclosure can be more fully understood, the following examples are set forth. It should be understood that these examples are for illustrative purposes only and are not to be construed as limiting this disclosure in any manner.
All materials are commercially available, for example from Sigma-Aldrich Chemical Company; Milwaukee, WI, or known to those skilled in the art unless otherwise stated or apparent. The following abbreviations are used in this section: L=liters, mL=milliliters, g=grams, min=minutes, rpm=revolutions per minute, sec=seconds, h=hours, mol =moles, mol %=mole percent, wt %=weight percent, nm=nanometer, μm=micrometer, mm=millimeter, cm=centimeter, ppm=parts per million, NMR=nuclear magnetic resonance, ° C.=degrees Celsius, kPa=kiloPascal, mW=milliWatt, kcps=thousand counts per second.
Results were obtained using the following test methods, unless otherwise noted.
Solid content was determined gravimetrically by placing samples of the dispersions on a heated balance and recording the mass before and after evaporation of solvent. The solid content was the ratio of the initial mass of the sample and the mass of the sample when the mass did not decrease further with continued heating.
The EW of a copolymer of TFE, a sulfonyl fluoride monomer (M2), and a vinyl ether or allyl ether monomer (M3) can be calculated by the formula:
19F-NMR spectra were used to determine the composition of the purified polymers. An NMR spectrometer available under the trade designation AVANCE II 300 from Bruker, Billerica, Mass., USA with a 5 mm Broadband probe was used. Samples of about 13 weight percent polymer dispersion were measured at 60° C.
Determination of Carboxyl Endgroups
A Fourier transform infrared spectroscopy (FT-IR) measurement can used to determine the number of carboxyl endgroups per 106 C-atoms in the copolymer. The measurement is performed by FT-IR in a transmission technique. The measured sample has a film thickness of 100 μm. The wave numbers of the
COOH peaks of interest are 1776 cm−1 and 1807 cm−1. The wave number of the C(O)F peak is 1885 cm1. (C(O)F will convert to a carboxyl group). To quantify the amount of carboxyl (C(O)F) endgroups of the polymer two IR spectra are taken. One from the carboxyl containing sample and one from a reference sample (without carboxyl groups).
The number of endgroups per 106 carbon atoms can be calculated via equation 1, 2 and 3 for F1, F2 and F3:
(peak high×F1)/film thickness [mm] (1)
(peak high×F2)/film thickness [mm] (2)
(peak high×F3)/film thickness [mm] (3)
with
F1: calculated factor related to the reference spectrum and ν=1776 cm−1
F2: calculated factor related to the reference spectrum and ν=1807 cm−1
F3: calculated factor related to the reference spectrum and ν=1885 cm−1
The sum of the results from the equations 1 to 3 yield the number of carboxyl endgroups per 106 carbon atoms.
The particle size determination was conducted by dynamic light scattering according to ISO 13321 (1996). A Zeta Sizer Nano ZS, available from Malvern Instruments Ltd, Malvern, Worcestershire, UK, equipped with a 50 mW laser operating at 532 nm was used for the analysis. 12 mm square glass cuvettes with round aperture and cap (PCS 8501, available from Malvern Instruments Ltd) were used to mount a sample volume of 1 mL. Since light scattering of surfactants is extremely sensitive to the presence of larger particles, e.g. dust particles, the presence of contaminants was minimized by thoroughly cleaning the cuvettes before the measurements. The cuvettes were washed with freshly-distilled acetone for 8 h in a cuvette washing device. Dust discipline was also applied to the samples by centrifuging the surfactant solutions in a laboratory centrifuge at 14,500 G (142,196 N/kg) for 10 min prior to the measurements. The measuring device was operated at 25° C. in 173° backscattering mode. Low correlation times of 1<1−6 sec were enabled by the research tool (the research tool is a software up-grade of the standard instrument provided by the supplier). In order to exploit the complete scattering ability of the sample volume, the following settings were applied in all cases: “attenuator,” 11; “measurement position,” 4.65 mm (center of the cell). Under these conditions, the baseline scattering of pure water (reference) is around 250 kcps. Each measurement consisting of 10 sub-runs was repeated for five times. The particle sizes are expressed as D50 value.
The melt flow index (MFI), reported in g/10 min, was measured with a Goettfert MPD, MI-Robo, MI4 melt indexer (Buchen, Germany) following a similar procedure to that described in DIN EN ISO 1133-1 at a support weight of 5.0 kg and a temperature of 265° C. The MFI was obtained with a standardized extrusion die of 2.1 mm in diameter and a length of 8.0 mm.
A TA Instruments AR2000 EX rheometer was used to measure the T(α) of the polymer samples. Samples were heated on a temperature ramp from −100° C. to about 125° C. at 2° C. per minute. Measurements were made at a frequency of one hertz.
A TA Instruments Q2000 DSC was used to measure the glass transition temperature (Tg) of the polymer samples. Samples were heated on a temperature ramp from −50° C. to about 200° C. at 10° C. per minute. Transition temperatures were analyzed on the second heats.
The oxygen permeability as a function of temperature for each membrane was determined using the time lag method. The membranes with an active area of 1 cm2 were placed in a permeability cell. Both chambers of the cell were subsequently evacuated for 6 hours. Time zero for the test coincided with the pressurization of upper chamber to 760 cm Hg with the challenging gas (oxygen). The variation of the pressure as a function of time in the evacuated lower chamber was measured using a pressure sensor (Baratron®, MKS, Mass., USA) with a sensitivity of 10−3 cm Hg.
The oxygen permeability P in barrer (cm3stp cm/sec cm2 cm Hg) was calculated using the following expression:
P=[Vb1/A T Rpa]dpb/dt
where Vb is the volume of the lower chamber in cm3, 1 is the membrane thickness in cm, A the exposed surface area of the membrane in cm2, T is temperature in ° K, pa is the pressure of the upper chamber in cm Hg, R is the gas constant (6236.367 cm Hg cm3/mol ° K), and dpb/dt is the rate of change of the pressure in the lower chamber as a function of time measured in the linear part of the pressure—time curve (cm Hg/sec).
The viscosities of the dispersions were measured using a TA Instruments AR2000ex rheometer equipped with a 1°, 60 mm cone fixture and a Peltier plate assembly. The measurement was done at 20° C. and a steady shear rate of 1 s−1. Data was taken every 10 seconds over a 60 second period, and the average is reported.
A polymer of tetrafluoroethylene (TFE), F2C═CF—O—CF2CF2CF2CF2SO2F (MV4S), and CF2═CF—O—(CF2)3—OCF3 (MV31) was prepared:
MV4S was prepared according to the method described in U.S. Pat. No. 6,624,328 (Guerra). MV31 was prepared according to the method described in U.S. Pat. No. 6,255,536 (Worm et al.)
A 4-L polymerization kettle equipped with an impeller agitator system was charged with ammonium oxalate monohydrate (5 g) and oxalic acid dihydrate (1 g) in H2O (2000 g) and 40 g of a 30 wt. % aqueous solution of CF3—O—(CF2)3—O—CFH—CF2—COONH4, prepared as described in “Preparation of Compound 11” in U.S. Pat. No. 7,671,112. The kettle was degassed and subsequently charged with nitrogen several times to assure that all of oxygen was removed. Afterwards, the kettle was purged with TFE, The kettle was then heated to 50° C. and the agitation system was set to 320 rpm. A mixture of MV4S (260 g), MV31 (50 g), and 8.6 g of the 30 Wt. % CF3—O—(CF2)3—O—CFH—CF2—COONH4 solution and deionized. water (165 g) were emulsified under high shear by an agitator available under the trade designation “ULTRA-TURRAX T 50” from IKA Works, Wilmington, N.C., USA operated at 24000 rpm for 2 min. The MV4S and MV31 emulsion was charged into the reaction kettle. The kettle was further charged with TFE (127 g) to a pressure of 6 bar (600 kPa). The polymerization was initiated by a 0.045% solution of KMnO4 (33 g) in deionized water. As the reaction started, the reaction temperature of 50° C. as well as the reaction pressure of 6 bar (600 kPa) were maintained by feeding TFE into the gas phase. After the first pressure drop, the continuous feeding of the MV4S and MV31 emulsion (in total 1037 g: 557 g MV4S and 106 g MV31 and 21 g of the 30% CF3—O—(CF2)3—O—CFH—CF2—COONH4 solution in 353 deionized. water), TFE (458 g), and of a 0.045% solution of KA/Malin deionized water (350 g) was continued. The molar ratio of the continuous feed was 72 mol % TFE, 23 mol MV4S and 5 mol % MV31. The average metering rate of the continuous addition of the 0.045% KMnO4 solution was 92 g/h. to obtain a polymer dispersion with a solid content of 23.2%. The polymerization time was 228 min. The latex particle diameter was 126 nm according to dynamic light scattering.
The polymer dispersion was charged into a 100L glass vessel equipped with a lab stirrer (PENDRAULIK). While the lab stirrer of the glass vessel was rotated to 2500 rpm, a 65 wt-% nitric acid (170 g) was fed continuously in the glass vessel to precipitate the polymer. Then the mixture was rotated for 1 h under the same stirring conditions with a final solid content of 1.4% in the polymerization medium (water phase).
The remaining aqueous polymerization medium was removed and the wet polymerization crumb was washed seven times with 4 L DI water while the stirrer was rotated to 930 rpm. The pH value of the seventh washing medium was nearly 4. The wet polymerizate was transferred in two portions in an air circulation dryer. Each portion was dried for 17 hours at 80° C. with a final water content of ≤0.1% determined by thermobalance.
The coagulated, washed, and dried polymer had a MFI (265° C./5 kg) of 41 g/10 min. The polymer had a composition of 70.3 mol % TFE, 24.4 mol-% MV4S and 5.3 mol MV31 as determined by 19F-NMR. spectroscopy measurements. This corresponds to an equivalent weight EW of 740. The glass transition temperature (Tg) was measured using the test method described above and found to be 3° C.
Hydrolysis of the polymer was done in a Parr 4554 2-Gallon Floor Stand Reactor equipped with a Parr 4848 Reactor Controller, 2700W Heater, a Parr Magnetic Drive Mixer, and a Neslab Thermoflex 2500 chiller for cooling. The reactor was charged with 1.5 L of deionized (DI) water, 24 g of LiOH*H2O, 14.1 g of Li2CO3, and 141 g of the polymer. The vessel was sealed, and the mixer was set to 300 rpm. The reactor was then heated to 255° C. over a period of 111 minutes. This temperature was held for 60 minutes. It was then cooled to 25° C. over 23 minutes, and upon reaching this temperature the mixer was shut off The dispersion was drained from the reactor into 4 L HDPE bottles and allowed to rest overnight.
The dispersion was passed through an ion exchange bed consisting of a Kimble Chromaflex Column with the dimensions of 38×500 mm filled with 300 mL of Amberlite IR-120(Plus) Hydrogen Form Ion Exchange Resin. The resin was prepared by first flushing the column with 3 L of DI water with the stop cock completely open. After 900 mL of 5% HC1 solution was passed through the column over 30 minutes followed by 600 mL of DI water over 20 minutes. Next 3 L of DI water was passed through with the stop cock fully open. The dispersion was then ion exchanged at a rate of 1200 mL per hour. Any precipitate that formed after hydrolysis was not fed into the ion exchange column. The resin was regenerated after every 400 mL of dispersion using the same process outlined above.
To dry the ionomer and prepare solvent and water based dispersions, 20 to 25 mL of the ion exchanged dispersion was placed into a 40-mL high density polyethylene (HDPE) bottle. The open bottle was placed in a muffle furnace set to 70° C. where it remained for 20 to 24 hours until the moisture content dropped below 10%, and the ionomer was a friable solid. Once the dispersion had dried, the final moisture content was determined, and n-propanol and DI H2O with 18.2 MOhm-cm resistivity were added. In this example 1.96 g of ionomer was combined with 4.32 g of n-propanol and 2.72 g of H2O to achieve a dispersion consisting of 20% ionomer, 48% n-propanol, and 32% water. The bottle was then placed on a roller set to 45 to 65 rpm for a period of 24 hours. A clear dispersion was formed with no visible undispersed material. The viscosity of the dispersion was 97 cps as determined using the test method above.
To make a membrane, dispersion was concentrated by rotary evaporation to near solids and then exposed to a stream of nitrogen gas. The dried ionomer was dispersed at 28-30 wt % into a 60/40 blend of n-propanol and water at room temperature. The solution was coated onto 2 mil (50.8 micrometer) thickness “KAPTON” polyimide liner secured to a glass substrate. The film was dried at 120° C. for 30 minutes and then transferred from the glass substrate to an aluminum pan. Drying was continued 140° C. for 15 minutes, ramped to 160° C. for 10 minutes, and then cooled to room temperature.
The T(α) was measured according to the test method above and determined to be 98° C.
The membrane was evaluated at 30° C. using the Oxygen Permeability evaluation method described above. A value of 161 (barrer×1010 was measured. The oxygen permeability at 50° C. and 70° C. was found to be higher than the detection limit.
A polymer of tetrafluoroethylene (TFE), F2C═CF—O—CF2CF2CF2CF2SO2F (MV4S), and CF2═CF—O—(CF2)3—OCF3 (MV31) was prepared:
MV4S and MV31 were prepared as described in Example 1.
A 4-L polymerization kettle equipped with an impeller agitator system was charged with ammonium oxalate monohydrate (5 g) and oxalic acid dihydrate (1 g) in H2O (2000 g) and 40 g of a 30 wt. % aqueous solution of CF3—O—(CF2)3—O—CFH—CF2—COONH4. The kettle was degassed and subsequently charged with nitrogen several times to assure that all of oxygen was removed.
Afterwards, the kettle was purged with TEE. The kettle was then heated to 50° C. and the agitation system was set to 320 rpm. A mixture of MV4S (237 g), MV31 (78 g), and 9.6 g of the 30 wt % CF3—O—(CF2)3—O—CFH—CF2—COONH4 solution and deionized water (147 g) were emulsified under high shear by an agitator available under the trade designation “ULTRA-TURRAX T 50” from IKA Works, operated at 24000 rpm for 2 min. The MV4S and MV31 emulsion was charged into the reaction kettle. The kettle was further charged with TFE (126 g) to a pressure of 6 bar (600 kPa), The polymerization was initiated by a 0.045% solution of KMna4 (20 g) irr deionized water. As the reaction started, the reaction temperature of 50 0C as well as the reaction pressure of 6 bar (600 kPa) were maintained by feeding TFE into the gas phase. After the first pressure drop, the continuous feeding of the MV4S and MV31 emulsion (in total 1128 g: 567 g MV4S and 187 g MV31 and 23 g of the 30% CF3—O—(CF2)3—O—CFH—CF2—COONH4-solution in 351 g deionized water), TEE (351 g), and of a 0.045% solution of KMnO4 in deionized water (120 g) was continued. The average metering rate of the continuous addition of the 0.045% KMnO4 solution was 37 g/h to obtain a polymer dispersion witha solid content of 19.7%. The polymerization time was 194 min, The latex particle diameter was 114 nm according to dynamic light scattering.
The copolymer was coagulated, washed, and dried similarly to Example 1. The coagulated, washed, and dried polymer had a MEI (265° C./5 kg) of 57 g/10 min. The calculated equivalent weight EW was 742.
A polymer of tetrafluoroethylene (TFE), F2C═CF—O—CF2CF2CF2CF2SO2F (MV4S), and CF2═CF—O—(CF2)2—CF3 (PPVE-1) was prepared:
A 4-L polymerization kettle with an impeller agitator system was charged with 5 g ammonium oxalate monohydrate and 1 g oxalic acid dihydrate in 2000 g H2O and 40 g of a 30 wt. % aqueous solution of CF3—O—(CF2)3—O—CFH—CF2—COONH4. The kettle was degassed and subsequently charged with nitrogen several times to assure that all of oxygen was removed. Afterwards, the kettle was purged with TEE. The kettle was then heated to 50° C. and the agitation system was set to 320 rpm. A mixture of 80 g MV4S, 2.7 g of a 30 wt. % CF3—O—(CF2)3—O—CFH—CF2—COONH4 solution and 51 g deionized water were emulsified under high shear by a “ULTRA-TURRAX T 50” agitator from IKA Works operated at 24000 rpm for 2 min. The MV4S-emulsion was charged into the reaction kettle. The kettle was further charged with 114 g
TEE and 40 g PPVE-1 to 6 bar pressure (600 kPa). The polymerization was initiated by 16 g of a 0.09% solution of potassium permanganate (104n04) in deionized water. As the reaction started, the reaction temperature of 50° C. as well as the reaction pressure of 6 bar (600 kPa) was maintained by feeding TEE and PPVE-1 into the gas phase. After the first pressure drop the continuous feeding of 190 g of the MV4S-emulsion (114 g MV4S and 4 g of a 30 wt. % CF3—O—(CF2)3—O—CFH-CF2—COONH4 solution in 72 deionized water). 193 g TFE, 121 g PPVE-1, and 235 g of a 0.09% solution of KMnO4 in deionized water was continued. The average metering rate of the continuously addition of the 0,09% KMnO4 solution was 123 g/h to obtain a polymer dispersion with a solid content of 14.1%. The polymerization time was 115 min and latex particle diameter was 150 nm according to dynamic light scattering.
The copolymer was coagulated, washed, and dried similarly to Example 1. The coagulated, washed, and dried polymer had a MFI (265° C./5 kg) of 66 g/10 min. The polymer showed a chemical composition of 74.2 mol-% TFE, 16.1 mol-% MV4S and 9.7 mol-% PPVE-1 as obtained by 19F-NMR-spectroscopy. This corresponds to an equivalent weight of 1000. The glass transition temperature (Tg) was measured using the test method described above and found to be 10° C.
The polymer was hydrolyzed similarly to Example 1 except 16.2 g of LiOH*H2O, 9.5 g of Li2CO3 and 129 g of the polymer was charged into the reactor. The reactor was then heated to 255° C. over a period of 114 minutes. The dispersion was ion exchanged, dried, and an n-propanol based dispersion was prepared similarly to Example 1. In Example 2, 2.14 g of ionomer was combined with 4.70 g of n-propanol and 2.96 g DI H2O. A clear dispersion was formed with no visible undispersed material. The viscosity of the dispersion was 41 cps as determined by the test method above.
A membrane was made similarly to Example 1. The T(α) was measured according to the test method above and determined to be 93° C. The membrane was evaluated at 30° C. using the Oxygen Permeability evaluation method described above. A value of 2.6 (barrer×1010) was measured. The oxygen permeability at 50° C. and 70° C. was found to be 5.8 and 10.1 (barrer×respectively.
A polymer of tetrafluoroethylene (TFE) and F2C═CF—O—CF2CF2CF2CF2SO2F (MV4S) was prepared:
MV4S was prepared as described above.
A 4-L polymerization kettle equipped with an impeller agitator system was charged with ammonium oxalate monohydrate (5 g) and oxalic acid dihydrate (1 g) in H2O (2000 g) and 40 g of a 30 wt. % aqueous solution of CF3—O—(CF2)3—O—CFH—CF2—COONH4. The kettle was degassed and subsequently charged with nitrogen several times to assure that all of oxygen was removed. Afterwards, the kettle was purged with TEE. The kettle was then heated to 50° C. and the agitation system was set to 320 rpm. A mixture of MV4S (200 g), 15 g of the 30 wt. % CF3—O—(CF2)3—O—CFH—-CF2—COONH4 solution and deionized water (360 g) were emulsified under high shear by an agitator available under the trade designation “ULTRA-TURRAX T 50” from KA Works operated at 24000 rpm for 2. nun. The MV4S emulsion was charged into the reaction kettle. The kettle was further charged with TFE (115 g) to a pressure of 6 bar (600 kPa). The polymerization was initiated by a 0.06% solution of KMnO4 (13 g) in deionized water. As the reaction started, the reaction temperature of 50° C. as well as the reaction pressure of 6 bar (600 kPa) were maintained by feeding TFE into the gas phase. After the first pressure drop, the continuous feeding of the MV4S emulsion (in total 1234 g: 630 g MV4S and 24 g of the 30% CF3—O—(CF2)3—O—CFH—CF2—COONH4-solution in 580 g deionized water), IFE (450 g), and of a 0.045% solution of KMnO4 in deionized water (297 g) was continued. The average metering rate of the continuous addition of the 0.06% KhmO4 solution was 80 g/h to obtain a polymer dispersion with a solid content of 22%. The polymerization tune was 232 min. The latex particle diameter was 75 nm according to dynamic light scattering.
4.1 kg of the polymer dispersion with a solid content of 22% was charged into a 10-L glass vessel equipped with a lab stirrer (PENDRAULIK). While the lab stirrer of the glass vessel was rotated to 2500 rpm, a 65 wt-% nitric acid (170 g) was fed continuously in the glass vessel to precipitate the polymer. Then the mixture was rotated for 1 h under the same stirring conditions with a final solid content of 1.4% in the polymerization medium (water phase). The remaining aqueous polymerization medium was removed and the wet polymerization crumb was washed seven times with 4 liter DI water while the stirrer was rotated to 930 rpm. The pH value of the seventh washing medium was nearly 4.
The wet polymerizate was transferred in two portions in an air circulation dryer. Each portion was dried for 17 hours at 80° C. with a final water content of ≤0.1% determined by thermobalance. The yield of dried polymer of the was 840 g.
The copolymer was coagulated, washed, and dried similarly to Example 1. The coagulated, washed, and dried polymer had a MFI (265° C./5 kg) of 38 g/10 min. The so-obtained polymer showed a chemical composition of 78 mol-% TYE, 22 mol-% MV4S as determined by 19F-NMR-spectroscopy. This corresponds to an equivalent weight of 734.
The polymer was hydrolyzed similarly to Example I except the reactor was charged with 4 L of DI water, 200 g of LiOH*H2O, 100 g of Li2CO3, and 1000 g of the polymer. The dispersion was ion exchanged and dried similarly to Example 1. A dispersion was prepared similarly to Example 1. The dispersion was clear with no visible undispersed material, however the dispersion was very viscous. The viscosity of the dispersion was 1472 cps as determined using the test method above.
To prepare a membrane, another dispersion consisting of 20 wt % solids dispersed in ethanol: water at a ratio 55:45 was prepared. A clear dispersion was formed with no visible undispersed material. The dispersion was coated similarly to Example 1 except the film was dried at 80° C. for 10 minutes and then at 200° C. for 15 minutes. The T(α) was measured according to the test method above and determined to be 104° C.
A dispersion consisting of 15 wt % ionomer, 46.75% n-propanol, and 38.25% water was prepared similarly to Example 1. A clear dispersion was formed with no visible undispersed material. A membrane was made similarly to Example 1 except the film was dried at 90° C. for 10 minutes and then at 100° C. for 15 minutes, and then ramped to 190° C. for 12 minutes, and then cooled to room temperature. The membrane was evaluated at 30° C. using the Oxygen Permeability evaluation method described above. A value of 0.64 (barrer×1010) was measured. The oxygen permeability at 50° C. and 70° C. was found to be 1.4 and 2.8 (barrer×1010), respectively.
A sample of AQUIVION D72-25BS aqueous dispersion was purchased from Sigma Aldrich. Approximately 16 mL was dried as described in Example 1. The equivalent weight of the polymer was reported to be 720 in the technical data sheet. The dried ionomer was redispersed at 15 wt% solids in n-propanol:water at a weight ratio of 60:40. The mixture formed a gel.
Various modifications and alterations of this disclosure may be made by those skilled in the art without departing from the scope and spirit of the disclosure, and it should be understood that this invention is not to be unduly limited to the illustrative embodiments set forth herein.
This application claims priority to U.S. Provisional Application Nos. 62/558,671 and 62/558,655, filed Sep. 14, 2017, and 62/730,648, filed Sep. 13, 2018, the disclosures of which are incorporated by reference in their entirety herein.
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/US2018/051096 | 9/14/2018 | WO | 00 |
| Number | Date | Country | |
|---|---|---|---|
| 62558655 | Sep 2017 | US | |
| 62558671 | Sep 2017 | US | |
| 62730648 | Sep 2018 | US |
