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US 20140162173A1
(19) United States
(12) Patent Application Publication (10) Pub. No.: US 2014/0162173 A1
Smith, JR. et al. (43) Pub. Date: Jun. 12, 2014
(54) SULFONATED (22) Filed: Jul. 20, 2013
PERFLUOROCYCLOPENTENYL POLYMERS _ _
AND USES THEREOF Related US. Application Data
(60) Provisional application No. 61/673,821, ?led on Jul.
(71) Applicant: The Board of Regents of the University 20, 2012~
of Texas System, Austin, TX (US)
Publication Classi?cation
(72) Inventors: Dennis W. Smith, JR., The Colony, TX
(US); Daniel K. Dei, Dallas, TX (US); (51) Int- Cl
John P Ferraris, Coppell, TX (US); H01M 8/10 (2006-01)
Kenneth J. Balkus, The Colony, TX C25B 13/08 (2006-01)
(US); Inga H. Musselman, Dallas, TX (52) U-s- Cl
Duck J_ Yang, Flower Mound, TX ..........(US); Grace Jones D. KalaW, Dallas, (2013-01); C25B 13/08 (2013-01)
TX (Us) (57) ABSTRACT
An aspect ofthe invention is directed to a polymer comprising
(73) Assignee: The Board of Regents of the University a SUlfonated Per?uorOCyCIOPemyl compound-“Other asPeCt
of Texas system, Austin, TX (Us) of the invention is directed to a sulfonated copolymer com
prising one or more sulfonated polymers. A further aspect of
the invention is directed to membranes prepared from the
(21) Appl. No.: 13/947,037 polymers ofthe claimed invention.
Sulfanalion
8035
PFcP-sogll
Soar;
Patent Application Publication Jun. 12, 2014 Sheet 1 0f 7 US 2014/0162173 Al
FIG. 2A
Patent Application Publication Jun. 12, 2014 Sheet 2 0f 7 US 2014/0162173 A1
R: ' er
FIG. 23
Patent Application Publication Jun. 12, 2014 Sheet 3 0f 7 US 2014/0162173 A1
FIG. 3
Patent Application Publication Jun. 12, 2014 Sheet 4 0f 7 US 2014/0162173 A1
F,“ F
F “ F
F F raspy “span
soy-x O l A i i, 0L
/  /  /  /
iOQAQ/ “ “so H “ F F _
3 F ><F I cross tinker
FIG. 4
Patent Application Publication Jun. 12, 2014 Sheet 5 0f 7 US 2014/0162173 A1
FIG. 5
US 2014/0162173 A1Jun. 12, 2014 Sheet 6 0f 7Patent Application Publication
mm
mm“.mmmm
mmmm»mmmgmgQMMm?mm”m3WWWmm“mm”mam
5......,,1.........Eifg2.1.0.5.}...in5.1.5.5......._..
w...
.ww.Ww
m1
,,a
Patent Application Publication Jun. 12, 2014 Sheet 7 0f 7 US 2014/0162173 A1
$1138
8&3
$35
7%
Suifonamd a
‘ £35 PNZEBF .Faiymer X
2%}
i3
Yempsmtwe {*8}
FIG. 7
US 2014/0162173 A1
SULFONATED
PERFLUOROCYCLOPENTENYL POLYMERS
AND USES THEREOF
CROSS-REFERENCES TO RELATED
APPLICATIONS
[0001] This application claims the bene?t of US. Provi
sional Application No. 61/673,821, ?led Jul. 20, 2012, which
is incorporated by reference as if fully set forth herein.
FIELD OF THE INVENTION
[0002] The claimed invention provides methods for the
synthesis ofsulfonated per?uorocyclic polymers and the sul
fonated polymers derived therefrom.
BACKGROUND OF THE INVENTION
[0003] Polymers with high levels of ?uorine have novel
properties including chemical and thermal resistance. The
commercialization of proton exchange membrane fuel cells
(PEMFCs) has been delayed due to the lack of a highly
e?icient and durable membrane material that can withstand
the harsh fuel cell operating conditions. The current PEM
standard is a per?uoroalkylsulfonic acid, Na?on®, which
displays chemical stability, mechanical resistance and a high
ionic conductivity of 0.1 S/cm at 80° C. and fully humidi?ed
conditions. Na?on®’s attractive PEM properties result from
its well-studied nanophase-separated morphology compris
ing hydrophilic and hydrophobic domain. Higher tempera
ture operation (21000 C.) forPEMFCs is advantageous due to
faster electrode kinetics of02 reduction, improved CO toler
ance of the catalyst, elimination of cathode side ?ooding at
high current throughput, and reduced radiator size in automo
biles. However, utility ofNa?on® at highertemperatures and
low relative humidity (550%) is limited due to the drastic
reduction of its proton conductivity resulting from dehydra
tion, its compromised mechanical strength, and its suscepti
bility to oxidative degradation by peroxide-derived free radi
cals formed under FC operation. Moreover, the proton
conducting hydrophilic domains in Na?on®’s structure
change unpredictably with changes in relative humidity and
temperature. Therefore, control of proton conductivity and
stability in PEMs are key factors being investigated to obtain
robust membranes at high temperature and low relative
humidity. The relationship between the proton conductivity
and membrane stability often leads to a trade-off, which has
become a majorproblem inPEM development. One approach
that has been investigated is the use of well-ordered block
copolymers that self-assemble into nanophases. Several
copolymer systems, such as sulfonated polysulfone-PVDF,
poly(arylene ether sulfone)/(sulfonated polybutadiene),
polysulfonated (styrene-butadiene), and sulfonated poly(sty
rene-isobutylene-styrene), have been reported.
[0004] Per?uorocyclic polymers are knownto display ther
mal/oxidative stability, durability, optical transparency, and
processability. The facile polymerization through a thermal
[2n+2rc] cycloaddition of the tri?uorovinyloxyether mono
mers affords the wide applicability ofthese polymers, includ
ing, gas separations and fuel cell membranes. However, with
the use ofper?uorocyclopentenyl (PFCP) monomer, the pro
duction ofthe resulting hompolymer, copolymer or terpoly
mer is cheaper than alternate monomers at least in part due to
the lack of need of high pressure equipment. Furthermore,
handling of PFCP monomer is safer, thereby making the
Jun. 12, 2014
synthesis ofthe polymer safer as well. Therefore, it would be
desirable to sulfonate per?uorocyclic polymers such as PFCP
for use in the manufacture of PEM membranes and other
desired applications.
SUMMARY OF THE INVENTION
[0005] An aspect of the invention is directed to a polymer
comprising a sulfonated per?uorocyclopentyl compound.
[0006] Another aspect of the invention is directed to a sul
fonated copolymer comprising one or more sulfonated poly
mers.
[0007] A further aspect ofthe invention is directed to mem
branes prepared from the sulfonated polymers ofthe claimed
invention.
BRIEF DESCRIPTION OF THE DRAWINGS
[0008] FIG. 1 shows a process for the sulfonation ofa PFCP
polymer in accordance with an embodiment ofthe invention;
[0009] FIG. 2A shows the synthesis for sulfonated PFCP
polymers using sulfonated monomers in accordance with an
embodiment of the invention;
[0010] FIG. 2B shows a synthesis process for sulfonated
PFCP monomers and polymers in accordance with an
embodiment of the invention;
[0011] FIGS. 3A and 3B show PFCP copolymers with high
sulfonation, chain functionalization and cross-linking poten
tial in accordance with an embodiment of the invention;
[0012] FIG. 4 illustrates the cross-linking of sulfonated
PFCP polymers in accordance with an embodiment of the
invention;
[0013] FIG. 5 shows the lHNMR (top) and 19P NMR (bot
tom) spectra for a PFCP-BP aryl etherhomopolymer in accor
dance with an embodiment of the invention;
[0014] FIG. 6 shows the 13C NMR spectrum for a PFCP-BP
aryl ether homopolymer in accordance with an embodiment
ofthe invention; and
[0015] FIG. 7 shows the comparative TGA thermograms of
a PFCP-BP polymer before and after sulfonation in accor
dance with an embodiment of the invention.
DETAILED DESCRIPTION OF EXEMPLARY
EMBODIMENTS
[0016] An embodiment ofthe claimed invention is directed
to the sulfonation of semi?uorinated polymers such as per
?uorocyclic polymers via a post-polymerization sulfonation
route. A further embodiment ofthe invention is directed to the
synthesis of sulfonated polymers using sulfonic acid-func
tionalized monomers. In certain embodiments of the inven
tion, the sulfonated polymers are per?uorocyclopentenyl
(PFCP) aromatic ether polymers.
[0017] In an embodiment of the invention, sulfonation of
polymers is performed using chlorosulfonic acid and thionyl
chloride. Another embodiment is directed to the use of sul
fonic acid-functionalized monomers in the synthesis of sul
fonated polymers.
[0018] A further embodiment ofthe invention is directed to
sulfonated PFCP copolymers prepared by the claimed meth
ods.
[0019] In an embodiment ofthe invention, PFCP polymers
are synthesized by the process set forth herein. To a dry round
bottom ?ask equipped with a magnetic stirrer, 2.97 mmol of
bisphenol, 6.54 mmol of triethylamine and 10 mL of DMF
were added. The solution was degassed with nitrogen for 10
US 2014/0162173 A1
min, and 2.97 mmol ofocta?uorocyclopentene was added via
syringe, after which the ?ask was heated slowly to 80° C. and
run for 24 h. Upon completion, the polymer was precipitated
in 100 mL of methanol, ?ltered, washed several times with
methanol, and dried under vacuum at 50° C. for 24 h giving a
white powder polymer.
[0020] In an embodiment of the invention, the molecular
weight of the resulting polymer ranges from 20,000 to 200,
000. In certain preferred embodiments, the molecular weight
ofthe resulting polymer ranges from 50,000 to 150,000.
[0021] Polymerization ofthe phenoxide salt (sulfonated or
nonsulfonated) with octa?uorocyclopentene (OFCP) mono
mer or with precursors is performed at a temperature ranging
from room temperature to 100° C. using solvents such as
DMF, mesitylene and bases such as triethylamine, sodium
hydride, cesium carbonate, dimethylamino pyridine, pyri
dine. The polymers are precipitated at room temperature with
methanol or water, followed by ?ltration, drying at 70° C. in
vacuum.
[0022] FIG. 1 shows the sulfonation ofa PFCP polymer. As
shown in FIG. 1, a solution of PFCP polymer (i.e. BP-PFCP)
in 100 mL of dichloromethane is placed in a 250-mL round
bottom ?ask equipped with a dropping funnel and N2 inlet/
outlet. Chlorosulfonic acid (48 mmol) is added dropwise at
room temperature. After 24 h, thionyl chloride (97 mmol) is
added, and the resulting solution is stirred for 2 d at room
temperature. To stop the reaction, a cold methanol/ice-water
mixture is pouredwith vigorous stirring into the mixture. The
sulfonated polymer is precipitated out at pH~5. The polymer
is collected by ?ltration, washed, and dried at 70° C. under
vacuum for 12 h. The application of this procedure can be
extended to a variety of other PFCP polymers.
[0023] As set forth in FIG. 2A, an alternate method for the
synthesis of a sulfonated PFCP involves the use of sulfonic
acid-functionalized monomers in the PFCP synthesis. The
polymerization of a sulfonated phenol and octa?uorocyclo
pentene (OFCP) form the sulfonated PFCP polymer. The
sulfonated bisphenol can be converted to its salt form by
washing with brine or the appropriate solution. In the usual
polymerization reaction, the sulfonated bisphenol in its salt
form is added to DMF in a reaction vessel/?ask. The solution
is degassed using a nitrogen purge and octa?uorocyclopen
tene is added. The reaction is slowly heated to 80° C. and
maintained for 24 h. The resulting polymer is collected by
precipitation in methanol, ?ltered, washed further with
methanol, and dried under vacuum at 50° C. for 24 h. The
sulfonate salt is converted to the sulfonic acid by washing the
polymer with water and hydrochloric acid. This strategy can
be expanded to encompass a wide range ofsulfonated bisphe
nols and potentially other dinucleophilic monomers (FIG.
2B).
[0024] An embodiment ofthe invention is directed to PFCP
copolymers with excellent thermal stability, processability,
chain modi?cation and cross-linking potential. FIG. 3A
shows the structure ofa triarylamine copolymer with a PFCP
biphenyl. The biphenyl groups are sulfonated for the PEMs
(proton exchange membranes) as indicated by the R groups,
while R2 serves as spacer groups depending on the desired
properties. Additionally, the triarylamine pendant chain can
be functionalized. Facile substitution at the R1 position pro
vides synthetic ?exibility for sulfonation or the addition of a
crosslinker. This is an advancement over PEMs for fuel cells
without crosslinking ability. The process is expected to
reduce membrane swelling, a well anticipated advantage over
Jun. 12, 2014
non-crosslinkable membranes. The copolymer shown in FIG.
3B has similar properties with functionalization on the biphe
nyl (sulfonation), as well as on the ?uorene pendant chain,
which can induce cross-linking.
[0025] The sulfonated PFCP polymer ofthe claimed inven
tion can be dissolved in aprotic, polar solvents such as DMSO
at a 5-10 wt % solution. In certain embodiments ofthe inven
tion, the sulfonated PFCP polymers are prepared as a ?lm by
solution casting onto a Te?on® substrate using a doctor blade
and an automatic ?lm applicator. The wet ?lm is dried under
vacuum following a temperature ramp with a ?nal annealing
at 180° C. for 24 h. The ?lm is kept in an environment with
controlled humidity until testing and characterization. The
?lms are soaked in a HCl/water solution for at least 12 h to
ensure that all sulfonic acid groups are acidi?ed.
[0026] Polymer blends of sulfonated and unsulfonated
PFCP polymers are prepared in different mole ratios (10:90,
20:80, 30:70, 50:50, 70:30, 80:20, 10:90). Each polymer is
?rst dissolved (5-10 wt %) separately in the same solvent (i.e.
DMSO) and stirred overnight to ensure dissolution. The poly
mers are then combined, stirred, and subjected to acoustic
mixing at 20% power for 20 min. The resulting polymer
blends are then cast as previously described.
[0027] Block copolymers of sulfonated and unsulfonated
PFCP polymers are cast as ?lms using a procedure similar to
that for pure sulfonated PFCP polymers.
[0028] In certain embodiments, electrospun ?bers of the
sulfonated PFCP polymer, embedded in a polymer blend
matrix are prepared using the following procedure: The sul
fonated PFCP polymer is ?rst electrospun into a nonwoven
mat of ?bers. These ?bers are then placed on a Te?on®
substrate. With the aid ofa doctor blade (set at a height higher
than the ?ber mat thickness), a polymer blend solution ofthe
sulfonated and unsulfonated PFCP is cast on the ?bers using
an automatic ?lm applicator. The same ?lm drying conditions
as previously described are followed for this system.
[0029] An important application for sulfonated PFCP poly
mers is theiruse as proton exchange membranes for fuel cells.
Due to the ease of sulfonation of the aromatic rings in PFCP
polymers, a high degree of acidity is obtained upon their
sulfonation. This acidity or hydrophilicity translates to
increased ion exchange capacity and proton conductivity
greater than or close to that of the current widely used PEM
material, Na?on® (IEC 0.91 meg/g, 00.1 S/cm at 80° C.,
550% R. H., respectively). Several systems based on the
sulfonated PFCP polymer for PEM materials are listedbelow:
1. Pure Sulfonated PFCP Homopolymers
[0030] The extent of sulfonation is highly controllable for
semi-?uorinated materials (i.e. PFCB polymers). To obtain
high proton conductivities greater than 0.1 S/cm, the PFCP
polymer is highly sulfonated without sacri?cing membrane
mechanical stability. To overcome membrane swelling
issues, the sulfonated PFCP polymer was crosslinked via the
reactive ?uorinated vinyl groups (FIG. 4). This approach of
using a highly sulfonated PFCP homopolymer increased pro
ton conductivity (20.10 S/cm).
2. Blends of Sulfonated and Unsulfonated PFCP
Homopolymers
[0031] To mimic Na?on®’s nanophase-separated mor
phology, sulfonated and unsulfonated PFCP homopolymers
were combined in polymer blends with different moles ratios.
US 2014/0162173 A1
Their combination provides the high proton conductivity of
the highly acidic hydrophilic PFCP polymer and the high
mechanical stability ofthe hydrophobic PFCP polymer in the
PEM. To further improve the PEM performance and lifetime,
the PFCP-based blends were crosslinked as previously
described.
3. Block Copolymers of Sulfonated and Unsulfonated PFCP
Polymers in Different Mole Ratios
[0032] Due to the ease ofchemistry and nature ofpolymer
ization ofPFCP, PFCP block copolymers were synthesized in
different block ratios of sulfonated (or hydrophilic) and pure
(or hydrophobic) PFCP homopolymers. Similar to blends,
these block copolymers provided high proton conductivity
without compromising the membrane mechanical integrity.
Without crosslinking, these block copolymers are expected to
be signi?cantly more stable than polymer blends at prolonged
fuel cell testing conditions (800 C., 250 R. H.). This strategy
increased membrane proton conductivity, performance and
lifetime.
[0033] 4. Electrospun Fibers of Sulfonated PFCP Embed
ded in a Polymer Blend Matrix ofthe Sulfonated and Unsul
fonated PFCP
[0034] The sulfonated PFCP polymer was electrospun into
a nonwoven mat of ?bers. These ?bers were then placed in a
polymer blend solution of the sulfonated and unsulfonated
PFCP. A distinct advantage of these electrospun sulfonated
PFCP (hydrophilic) nano?bers in nanophase-separated
matrices over pure block copolymer membranes is the lack of
need for physical control over the domain sizes. Rather than
using blocks, domain sizes are controlled by adjusting the
?ber diameter and density. The proton transport is easier via
the acidic sites along the ?ber and in the matrix, without
sacri?cing the integrity of the membrane. This strategy sig
ni?cantly increased PEM fuel cell performance and lifetime.
[0035] The polymer membranes of the claimed invention
possess a higher IEC and greater chemical and thermal sta
bility relative to currently existing alternatives. Due to the
inexpensive cost ofproduction and synthesis, the membranes
of the claimed invention lend themselves to commercializa
tion for fuel cell production.
WORKING EXAMPLES
Synthesis of PFCP-BP Homopolymer
[0036] In a 25 mL Schlenk tube equipped with a magnetic
stirrer was added 2.97 mmol of Biphenol, 6.54 mmol of
triethylamine and 2 mL of DMF. The solution was degassed
with nitrogen for 10 min and 2.97 mmol of octa?uorocyclo
pentene was added via syringe and the Schlenk ?ask was
heated slowly to 800 C. for 24 h. The polymer was then
precipitated in 100 mL of methanol, ?ltered, washed several
time with methanol and dried under vaccum at 50° C. for 24
h giving a white powder (yield:50%). FIG. 5 shows the
lHNMR (top) and 19P NMR (bottom) spectra for a PFCP-BP
aryl ether homopolymer. FIG. 6 shows the 13C NMR spec
trum for a PFCP-BP aryl ether homopolymer. The NMR
values obtained were: 1H NMR (400 MHz, acetone-d6, 6):
6.92 (dm, 3JH_2(H_1):8.58 Hz, 4H), 7.31 (dm, 3.LLI_1(H_2):8.58
Hz, 4H); 19P NMR (376 MHz, acetone-d6, 6): —113.89 (4F),
—129.60 (2F); 13C NMR (100 MHz, acetone-d6, 6): 110.5
(PFCP, CF2), 114.0 (PFCP, CF2), 118.5, 128.8, 135.0 (PFCP,
C:C), 137.7, 154.5. FTIR (v, cm-1) data obtained was as
Jun. 12, 2014
follows: 3151 and 3070 (H%:C), 2941 (CiH), 1729
(C:C), 1270 (CiO), 1150 (CiF), 780 and 653 (CiF).
The molecular weight of the homopolymer obtained in this
process was 29,800.
Sulfonation of PFCP-BP Homopolymer
[0037] PFCP-BP polymer was sulfonated using chlorosul
fonic acid and thionyl chloride. PFCP-BP copolymer (3.0 g,
9 mmol) and dichloromethane (100 mL) were placed in a
250-mL round bottom ?ask equipped with a dropping funnel
and N2 inlet/outlet. Chlorosulfonic acid (28 mL, 430 mmol)
was added dropwise at room temperature. After 24 h, thionyl
chloride (61 mL, 870 mmol) was added, and the resulting
solution was stirred for 2 days at room temperature. The
reaction was terminated by the slow addition ofa cold metha
nol/ice-watermixture accompanied by vigorous stirring. The
sulfonated PFCP-BP polymer precipitated out around pH 5.
The polymer was collected by ?ltration and washed several
times with water until the washings were neutral. The result
ing yellow polymer obtained was dried at 60° C. under
vacuum for 12 hrs. (yield: 81%). FIG. 7 shows the compara
tive TGA thermograms of a PFCP-BP polymer before and
after sulfonation in accordance with an embodiment of the
invention.
What is claimed is:
1. A polymer, wherein the polymer comprises a sulfonated
per?uorocyclopentyl compound.
2. The polymer ofclaim 1, wherein the sulfonated per?uo
rocyclopentyl compound is selected from:
Ar I F, — O — Ar]
Ar] I sulfonated phenols ofphenyl, biphenyl, triphenyl, triarylamine, ?uorene.
US 2014/0162173 A1
3. The polymer ofclaim 1, wherein the sulfonated per?uo
rocyclopentenyl compound is synthesized by the reaction:
F F
F F
F F
Sulfonation
0 Al O —>
Y!
F
4. The polymer ofclaim wherein the sulfonated per?uoro
cyclopentenyl compound is synthesized by the reaction:
F F
F F
+
F F
F F
HO A OH
1 NEt3
DMF
H038 SO3H 10 h, so 0.
F F
F F
F F
o A1 0%n
H038 SO3H
A1 I — (BF), — C(CH3)2 _ , C(CF3)2, — SOz _
Jun. 12, 2014
5. The polymer ofclaim 1, wherein the polymer comprises
a copolymer comprising:
Block A
F F
F F
F F
O O
SO3H SO3H
Block B
F F
F F
F F
m
Block C
F F
F F
F F
Ar; I sulfonated or nonsulfonated phenyl, biphenyl, triphenyl, triarylamine, ?uorene.
6. The polymer of claim 5, wherein the copolymer is a
homopolymer.
7. The polymer of claim 5, wherein the copolymer is a
heteropolymer.
8. The polymer of claim 5, wherein the copolymer is sul
fonated.
9. The polymer of claim 1 wherein said polymer has a
molecular weight ranging from 20,000 to 200,000.
10. The polymer of claim 9 wherein said polymer has a
molecular weight ranging from 50,000 to 150,000.
11. A membrane comprising the polymer of claim 1.
12. The membrane of claim 11, wherein the membrane
further comprises a non-sulfonated per?uorocyclopentenyl
compound.
13. The membrane of claim 11, wherein the membrane
comprises e-spun ?bers comprising the polymer of claim 1.
14. The membrane of claim 11, wherein the membrane is
extruded from a powder form of the polymer.
15. The membrane of claim 11, wherein the membrane is
prepared by wetting a mat of e-spun ?bers.
16. The membrane of claim 11, wherein the membrane is
used in fuel cells, ion exchange resins, and for electrolysis
applications.

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Sulfonated perfluorocyclopentenyl polymers and uses thereof

  • 1. US 20140162173A1 (19) United States (12) Patent Application Publication (10) Pub. No.: US 2014/0162173 A1 Smith, JR. et al. (43) Pub. Date: Jun. 12, 2014 (54) SULFONATED (22) Filed: Jul. 20, 2013 PERFLUOROCYCLOPENTENYL POLYMERS _ _ AND USES THEREOF Related US. Application Data (60) Provisional application No. 61/673,821, ?led on Jul. (71) Applicant: The Board of Regents of the University 20, 2012~ of Texas System, Austin, TX (US) Publication Classi?cation (72) Inventors: Dennis W. Smith, JR., The Colony, TX (US); Daniel K. Dei, Dallas, TX (US); (51) Int- Cl John P Ferraris, Coppell, TX (US); H01M 8/10 (2006-01) Kenneth J. Balkus, The Colony, TX C25B 13/08 (2006-01) (US); Inga H. Musselman, Dallas, TX (52) U-s- Cl Duck J_ Yang, Flower Mound, TX ..........(US); Grace Jones D. KalaW, Dallas, (2013-01); C25B 13/08 (2013-01) TX (Us) (57) ABSTRACT An aspect ofthe invention is directed to a polymer comprising (73) Assignee: The Board of Regents of the University a SUlfonated Per?uorOCyCIOPemyl compound-“Other asPeCt of Texas system, Austin, TX (Us) of the invention is directed to a sulfonated copolymer com prising one or more sulfonated polymers. A further aspect of the invention is directed to membranes prepared from the (21) Appl. No.: 13/947,037 polymers ofthe claimed invention. Sulfanalion 8035 PFcP-sogll Soar;
  • 2. Patent Application Publication Jun. 12, 2014 Sheet 1 0f 7 US 2014/0162173 Al FIG. 2A
  • 3. Patent Application Publication Jun. 12, 2014 Sheet 2 0f 7 US 2014/0162173 A1 R: ' er FIG. 23
  • 4. Patent Application Publication Jun. 12, 2014 Sheet 3 0f 7 US 2014/0162173 A1 FIG. 3
  • 5. Patent Application Publication Jun. 12, 2014 Sheet 4 0f 7 US 2014/0162173 A1 F,“ F F “ F F F raspy “span soy-x O l A i i, 0L / / / / iOQAQ/ “ “so H “ F F _ 3 F ><F I cross tinker FIG. 4
  • 6. Patent Application Publication Jun. 12, 2014 Sheet 5 0f 7 US 2014/0162173 A1 FIG. 5
  • 7. US 2014/0162173 A1Jun. 12, 2014 Sheet 6 0f 7Patent Application Publication mm mm“.mmmm mmmm»mmmgmgQMMm?mm”m3WWWmm“mm”mam 5......,,1.........Eifg2.1.0.5.}...in5.1.5.5......._.. w... .ww.Ww m1 ,,a
  • 8. Patent Application Publication Jun. 12, 2014 Sheet 7 0f 7 US 2014/0162173 A1 $1138 8&3 $35 7% Suifonamd a ‘ £35 PNZEBF .Faiymer X 2%} i3 Yempsmtwe {*8} FIG. 7
  • 9. US 2014/0162173 A1 SULFONATED PERFLUOROCYCLOPENTENYL POLYMERS AND USES THEREOF CROSS-REFERENCES TO RELATED APPLICATIONS [0001] This application claims the bene?t of US. Provi sional Application No. 61/673,821, ?led Jul. 20, 2012, which is incorporated by reference as if fully set forth herein. FIELD OF THE INVENTION [0002] The claimed invention provides methods for the synthesis ofsulfonated per?uorocyclic polymers and the sul fonated polymers derived therefrom. BACKGROUND OF THE INVENTION [0003] Polymers with high levels of ?uorine have novel properties including chemical and thermal resistance. The commercialization of proton exchange membrane fuel cells (PEMFCs) has been delayed due to the lack of a highly e?icient and durable membrane material that can withstand the harsh fuel cell operating conditions. The current PEM standard is a per?uoroalkylsulfonic acid, Na?on®, which displays chemical stability, mechanical resistance and a high ionic conductivity of 0.1 S/cm at 80° C. and fully humidi?ed conditions. Na?on®’s attractive PEM properties result from its well-studied nanophase-separated morphology compris ing hydrophilic and hydrophobic domain. Higher tempera ture operation (21000 C.) forPEMFCs is advantageous due to faster electrode kinetics of02 reduction, improved CO toler ance of the catalyst, elimination of cathode side ?ooding at high current throughput, and reduced radiator size in automo biles. However, utility ofNa?on® at highertemperatures and low relative humidity (550%) is limited due to the drastic reduction of its proton conductivity resulting from dehydra tion, its compromised mechanical strength, and its suscepti bility to oxidative degradation by peroxide-derived free radi cals formed under FC operation. Moreover, the proton conducting hydrophilic domains in Na?on®’s structure change unpredictably with changes in relative humidity and temperature. Therefore, control of proton conductivity and stability in PEMs are key factors being investigated to obtain robust membranes at high temperature and low relative humidity. The relationship between the proton conductivity and membrane stability often leads to a trade-off, which has become a majorproblem inPEM development. One approach that has been investigated is the use of well-ordered block copolymers that self-assemble into nanophases. Several copolymer systems, such as sulfonated polysulfone-PVDF, poly(arylene ether sulfone)/(sulfonated polybutadiene), polysulfonated (styrene-butadiene), and sulfonated poly(sty rene-isobutylene-styrene), have been reported. [0004] Per?uorocyclic polymers are knownto display ther mal/oxidative stability, durability, optical transparency, and processability. The facile polymerization through a thermal [2n+2rc] cycloaddition of the tri?uorovinyloxyether mono mers affords the wide applicability ofthese polymers, includ ing, gas separations and fuel cell membranes. However, with the use ofper?uorocyclopentenyl (PFCP) monomer, the pro duction ofthe resulting hompolymer, copolymer or terpoly mer is cheaper than alternate monomers at least in part due to the lack of need of high pressure equipment. Furthermore, handling of PFCP monomer is safer, thereby making the Jun. 12, 2014 synthesis ofthe polymer safer as well. Therefore, it would be desirable to sulfonate per?uorocyclic polymers such as PFCP for use in the manufacture of PEM membranes and other desired applications. SUMMARY OF THE INVENTION [0005] An aspect of the invention is directed to a polymer comprising a sulfonated per?uorocyclopentyl compound. [0006] Another aspect of the invention is directed to a sul fonated copolymer comprising one or more sulfonated poly mers. [0007] A further aspect ofthe invention is directed to mem branes prepared from the sulfonated polymers ofthe claimed invention. BRIEF DESCRIPTION OF THE DRAWINGS [0008] FIG. 1 shows a process for the sulfonation ofa PFCP polymer in accordance with an embodiment ofthe invention; [0009] FIG. 2A shows the synthesis for sulfonated PFCP polymers using sulfonated monomers in accordance with an embodiment of the invention; [0010] FIG. 2B shows a synthesis process for sulfonated PFCP monomers and polymers in accordance with an embodiment of the invention; [0011] FIGS. 3A and 3B show PFCP copolymers with high sulfonation, chain functionalization and cross-linking poten tial in accordance with an embodiment of the invention; [0012] FIG. 4 illustrates the cross-linking of sulfonated PFCP polymers in accordance with an embodiment of the invention; [0013] FIG. 5 shows the lHNMR (top) and 19P NMR (bot tom) spectra for a PFCP-BP aryl etherhomopolymer in accor dance with an embodiment of the invention; [0014] FIG. 6 shows the 13C NMR spectrum for a PFCP-BP aryl ether homopolymer in accordance with an embodiment ofthe invention; and [0015] FIG. 7 shows the comparative TGA thermograms of a PFCP-BP polymer before and after sulfonation in accor dance with an embodiment of the invention. DETAILED DESCRIPTION OF EXEMPLARY EMBODIMENTS [0016] An embodiment ofthe claimed invention is directed to the sulfonation of semi?uorinated polymers such as per ?uorocyclic polymers via a post-polymerization sulfonation route. A further embodiment ofthe invention is directed to the synthesis of sulfonated polymers using sulfonic acid-func tionalized monomers. In certain embodiments of the inven tion, the sulfonated polymers are per?uorocyclopentenyl (PFCP) aromatic ether polymers. [0017] In an embodiment of the invention, sulfonation of polymers is performed using chlorosulfonic acid and thionyl chloride. Another embodiment is directed to the use of sul fonic acid-functionalized monomers in the synthesis of sul fonated polymers. [0018] A further embodiment ofthe invention is directed to sulfonated PFCP copolymers prepared by the claimed meth ods. [0019] In an embodiment ofthe invention, PFCP polymers are synthesized by the process set forth herein. To a dry round bottom ?ask equipped with a magnetic stirrer, 2.97 mmol of bisphenol, 6.54 mmol of triethylamine and 10 mL of DMF were added. The solution was degassed with nitrogen for 10
  • 10. US 2014/0162173 A1 min, and 2.97 mmol ofocta?uorocyclopentene was added via syringe, after which the ?ask was heated slowly to 80° C. and run for 24 h. Upon completion, the polymer was precipitated in 100 mL of methanol, ?ltered, washed several times with methanol, and dried under vacuum at 50° C. for 24 h giving a white powder polymer. [0020] In an embodiment of the invention, the molecular weight of the resulting polymer ranges from 20,000 to 200, 000. In certain preferred embodiments, the molecular weight ofthe resulting polymer ranges from 50,000 to 150,000. [0021] Polymerization ofthe phenoxide salt (sulfonated or nonsulfonated) with octa?uorocyclopentene (OFCP) mono mer or with precursors is performed at a temperature ranging from room temperature to 100° C. using solvents such as DMF, mesitylene and bases such as triethylamine, sodium hydride, cesium carbonate, dimethylamino pyridine, pyri dine. The polymers are precipitated at room temperature with methanol or water, followed by ?ltration, drying at 70° C. in vacuum. [0022] FIG. 1 shows the sulfonation ofa PFCP polymer. As shown in FIG. 1, a solution of PFCP polymer (i.e. BP-PFCP) in 100 mL of dichloromethane is placed in a 250-mL round bottom ?ask equipped with a dropping funnel and N2 inlet/ outlet. Chlorosulfonic acid (48 mmol) is added dropwise at room temperature. After 24 h, thionyl chloride (97 mmol) is added, and the resulting solution is stirred for 2 d at room temperature. To stop the reaction, a cold methanol/ice-water mixture is pouredwith vigorous stirring into the mixture. The sulfonated polymer is precipitated out at pH~5. The polymer is collected by ?ltration, washed, and dried at 70° C. under vacuum for 12 h. The application of this procedure can be extended to a variety of other PFCP polymers. [0023] As set forth in FIG. 2A, an alternate method for the synthesis of a sulfonated PFCP involves the use of sulfonic acid-functionalized monomers in the PFCP synthesis. The polymerization of a sulfonated phenol and octa?uorocyclo pentene (OFCP) form the sulfonated PFCP polymer. The sulfonated bisphenol can be converted to its salt form by washing with brine or the appropriate solution. In the usual polymerization reaction, the sulfonated bisphenol in its salt form is added to DMF in a reaction vessel/?ask. The solution is degassed using a nitrogen purge and octa?uorocyclopen tene is added. The reaction is slowly heated to 80° C. and maintained for 24 h. The resulting polymer is collected by precipitation in methanol, ?ltered, washed further with methanol, and dried under vacuum at 50° C. for 24 h. The sulfonate salt is converted to the sulfonic acid by washing the polymer with water and hydrochloric acid. This strategy can be expanded to encompass a wide range ofsulfonated bisphe nols and potentially other dinucleophilic monomers (FIG. 2B). [0024] An embodiment ofthe invention is directed to PFCP copolymers with excellent thermal stability, processability, chain modi?cation and cross-linking potential. FIG. 3A shows the structure ofa triarylamine copolymer with a PFCP biphenyl. The biphenyl groups are sulfonated for the PEMs (proton exchange membranes) as indicated by the R groups, while R2 serves as spacer groups depending on the desired properties. Additionally, the triarylamine pendant chain can be functionalized. Facile substitution at the R1 position pro vides synthetic ?exibility for sulfonation or the addition of a crosslinker. This is an advancement over PEMs for fuel cells without crosslinking ability. The process is expected to reduce membrane swelling, a well anticipated advantage over Jun. 12, 2014 non-crosslinkable membranes. The copolymer shown in FIG. 3B has similar properties with functionalization on the biphe nyl (sulfonation), as well as on the ?uorene pendant chain, which can induce cross-linking. [0025] The sulfonated PFCP polymer ofthe claimed inven tion can be dissolved in aprotic, polar solvents such as DMSO at a 5-10 wt % solution. In certain embodiments ofthe inven tion, the sulfonated PFCP polymers are prepared as a ?lm by solution casting onto a Te?on® substrate using a doctor blade and an automatic ?lm applicator. The wet ?lm is dried under vacuum following a temperature ramp with a ?nal annealing at 180° C. for 24 h. The ?lm is kept in an environment with controlled humidity until testing and characterization. The ?lms are soaked in a HCl/water solution for at least 12 h to ensure that all sulfonic acid groups are acidi?ed. [0026] Polymer blends of sulfonated and unsulfonated PFCP polymers are prepared in different mole ratios (10:90, 20:80, 30:70, 50:50, 70:30, 80:20, 10:90). Each polymer is ?rst dissolved (5-10 wt %) separately in the same solvent (i.e. DMSO) and stirred overnight to ensure dissolution. The poly mers are then combined, stirred, and subjected to acoustic mixing at 20% power for 20 min. The resulting polymer blends are then cast as previously described. [0027] Block copolymers of sulfonated and unsulfonated PFCP polymers are cast as ?lms using a procedure similar to that for pure sulfonated PFCP polymers. [0028] In certain embodiments, electrospun ?bers of the sulfonated PFCP polymer, embedded in a polymer blend matrix are prepared using the following procedure: The sul fonated PFCP polymer is ?rst electrospun into a nonwoven mat of ?bers. These ?bers are then placed on a Te?on® substrate. With the aid ofa doctor blade (set at a height higher than the ?ber mat thickness), a polymer blend solution ofthe sulfonated and unsulfonated PFCP is cast on the ?bers using an automatic ?lm applicator. The same ?lm drying conditions as previously described are followed for this system. [0029] An important application for sulfonated PFCP poly mers is theiruse as proton exchange membranes for fuel cells. Due to the ease of sulfonation of the aromatic rings in PFCP polymers, a high degree of acidity is obtained upon their sulfonation. This acidity or hydrophilicity translates to increased ion exchange capacity and proton conductivity greater than or close to that of the current widely used PEM material, Na?on® (IEC 0.91 meg/g, 00.1 S/cm at 80° C., 550% R. H., respectively). Several systems based on the sulfonated PFCP polymer for PEM materials are listedbelow: 1. Pure Sulfonated PFCP Homopolymers [0030] The extent of sulfonation is highly controllable for semi-?uorinated materials (i.e. PFCB polymers). To obtain high proton conductivities greater than 0.1 S/cm, the PFCP polymer is highly sulfonated without sacri?cing membrane mechanical stability. To overcome membrane swelling issues, the sulfonated PFCP polymer was crosslinked via the reactive ?uorinated vinyl groups (FIG. 4). This approach of using a highly sulfonated PFCP homopolymer increased pro ton conductivity (20.10 S/cm). 2. Blends of Sulfonated and Unsulfonated PFCP Homopolymers [0031] To mimic Na?on®’s nanophase-separated mor phology, sulfonated and unsulfonated PFCP homopolymers were combined in polymer blends with different moles ratios.
  • 11. US 2014/0162173 A1 Their combination provides the high proton conductivity of the highly acidic hydrophilic PFCP polymer and the high mechanical stability ofthe hydrophobic PFCP polymer in the PEM. To further improve the PEM performance and lifetime, the PFCP-based blends were crosslinked as previously described. 3. Block Copolymers of Sulfonated and Unsulfonated PFCP Polymers in Different Mole Ratios [0032] Due to the ease ofchemistry and nature ofpolymer ization ofPFCP, PFCP block copolymers were synthesized in different block ratios of sulfonated (or hydrophilic) and pure (or hydrophobic) PFCP homopolymers. Similar to blends, these block copolymers provided high proton conductivity without compromising the membrane mechanical integrity. Without crosslinking, these block copolymers are expected to be signi?cantly more stable than polymer blends at prolonged fuel cell testing conditions (800 C., 250 R. H.). This strategy increased membrane proton conductivity, performance and lifetime. [0033] 4. Electrospun Fibers of Sulfonated PFCP Embed ded in a Polymer Blend Matrix ofthe Sulfonated and Unsul fonated PFCP [0034] The sulfonated PFCP polymer was electrospun into a nonwoven mat of ?bers. These ?bers were then placed in a polymer blend solution of the sulfonated and unsulfonated PFCP. A distinct advantage of these electrospun sulfonated PFCP (hydrophilic) nano?bers in nanophase-separated matrices over pure block copolymer membranes is the lack of need for physical control over the domain sizes. Rather than using blocks, domain sizes are controlled by adjusting the ?ber diameter and density. The proton transport is easier via the acidic sites along the ?ber and in the matrix, without sacri?cing the integrity of the membrane. This strategy sig ni?cantly increased PEM fuel cell performance and lifetime. [0035] The polymer membranes of the claimed invention possess a higher IEC and greater chemical and thermal sta bility relative to currently existing alternatives. Due to the inexpensive cost ofproduction and synthesis, the membranes of the claimed invention lend themselves to commercializa tion for fuel cell production. WORKING EXAMPLES Synthesis of PFCP-BP Homopolymer [0036] In a 25 mL Schlenk tube equipped with a magnetic stirrer was added 2.97 mmol of Biphenol, 6.54 mmol of triethylamine and 2 mL of DMF. The solution was degassed with nitrogen for 10 min and 2.97 mmol of octa?uorocyclo pentene was added via syringe and the Schlenk ?ask was heated slowly to 800 C. for 24 h. The polymer was then precipitated in 100 mL of methanol, ?ltered, washed several time with methanol and dried under vaccum at 50° C. for 24 h giving a white powder (yield:50%). FIG. 5 shows the lHNMR (top) and 19P NMR (bottom) spectra for a PFCP-BP aryl ether homopolymer. FIG. 6 shows the 13C NMR spec trum for a PFCP-BP aryl ether homopolymer. The NMR values obtained were: 1H NMR (400 MHz, acetone-d6, 6): 6.92 (dm, 3JH_2(H_1):8.58 Hz, 4H), 7.31 (dm, 3.LLI_1(H_2):8.58 Hz, 4H); 19P NMR (376 MHz, acetone-d6, 6): —113.89 (4F), —129.60 (2F); 13C NMR (100 MHz, acetone-d6, 6): 110.5 (PFCP, CF2), 114.0 (PFCP, CF2), 118.5, 128.8, 135.0 (PFCP, C:C), 137.7, 154.5. FTIR (v, cm-1) data obtained was as Jun. 12, 2014 follows: 3151 and 3070 (H%:C), 2941 (CiH), 1729 (C:C), 1270 (CiO), 1150 (CiF), 780 and 653 (CiF). The molecular weight of the homopolymer obtained in this process was 29,800. Sulfonation of PFCP-BP Homopolymer [0037] PFCP-BP polymer was sulfonated using chlorosul fonic acid and thionyl chloride. PFCP-BP copolymer (3.0 g, 9 mmol) and dichloromethane (100 mL) were placed in a 250-mL round bottom ?ask equipped with a dropping funnel and N2 inlet/outlet. Chlorosulfonic acid (28 mL, 430 mmol) was added dropwise at room temperature. After 24 h, thionyl chloride (61 mL, 870 mmol) was added, and the resulting solution was stirred for 2 days at room temperature. The reaction was terminated by the slow addition ofa cold metha nol/ice-watermixture accompanied by vigorous stirring. The sulfonated PFCP-BP polymer precipitated out around pH 5. The polymer was collected by ?ltration and washed several times with water until the washings were neutral. The result ing yellow polymer obtained was dried at 60° C. under vacuum for 12 hrs. (yield: 81%). FIG. 7 shows the compara tive TGA thermograms of a PFCP-BP polymer before and after sulfonation in accordance with an embodiment of the invention. What is claimed is: 1. A polymer, wherein the polymer comprises a sulfonated per?uorocyclopentyl compound. 2. The polymer ofclaim 1, wherein the sulfonated per?uo rocyclopentyl compound is selected from: Ar I F, — O — Ar] Ar] I sulfonated phenols ofphenyl, biphenyl, triphenyl, triarylamine, ?uorene.
  • 12. US 2014/0162173 A1 3. The polymer ofclaim 1, wherein the sulfonated per?uo rocyclopentenyl compound is synthesized by the reaction: F F F F F F Sulfonation 0 Al O —> Y! F 4. The polymer ofclaim wherein the sulfonated per?uoro cyclopentenyl compound is synthesized by the reaction: F F F F + F F F F HO A OH 1 NEt3 DMF H038 SO3H 10 h, so 0. F F F F F F o A1 0%n H038 SO3H A1 I — (BF), — C(CH3)2 _ , C(CF3)2, — SOz _ Jun. 12, 2014 5. The polymer ofclaim 1, wherein the polymer comprises a copolymer comprising: Block A F F F F F F O O SO3H SO3H Block B F F F F F F m Block C F F F F F F Ar; I sulfonated or nonsulfonated phenyl, biphenyl, triphenyl, triarylamine, ?uorene. 6. The polymer of claim 5, wherein the copolymer is a homopolymer. 7. The polymer of claim 5, wherein the copolymer is a heteropolymer. 8. The polymer of claim 5, wherein the copolymer is sul fonated. 9. The polymer of claim 1 wherein said polymer has a molecular weight ranging from 20,000 to 200,000. 10. The polymer of claim 9 wherein said polymer has a molecular weight ranging from 50,000 to 150,000. 11. A membrane comprising the polymer of claim 1. 12. The membrane of claim 11, wherein the membrane further comprises a non-sulfonated per?uorocyclopentenyl compound. 13. The membrane of claim 11, wherein the membrane comprises e-spun ?bers comprising the polymer of claim 1. 14. The membrane of claim 11, wherein the membrane is extruded from a powder form of the polymer. 15. The membrane of claim 11, wherein the membrane is prepared by wetting a mat of e-spun ?bers. 16. The membrane of claim 11, wherein the membrane is used in fuel cells, ion exchange resins, and for electrolysis applications.