U.S. patent application number 13/521105 was filed with the patent office on 2013-12-19 for anionic exchange electrolyte polymer membranes.
This patent application is currently assigned to DAIS ANALYTIC CORPORATION. The applicant listed for this patent is Timothy Tangredi. Invention is credited to Scott G. Ehrenberg, Timothy Tangredi.
Application Number | 20130338244 13/521105 |
Document ID | / |
Family ID | 44306164 |
Filed Date | 2013-12-19 |
United States Patent
Application |
20130338244 |
Kind Code |
A9 |
Ehrenberg; Scott G. ; et
al. |
December 19, 2013 |
ANIONIC EXCHANGE ELECTROLYTE POLYMER MEMBRANES
Abstract
The present disclosure provides a membrane having a first major
surface and a second major surface and including one or more
anionic exchange electrolyte polymers. The membranes can be useful
for selectively mass transporting molecules and/or ions.
Inventors: |
Ehrenberg; Scott G.; (Port
Richey, FL) ; Tangredi; Timothy; (Trinity,
FL) |
|
Applicant: |
Name |
City |
State |
Country |
Type |
Tangredi; Timothy |
Trinity |
FL |
US |
|
|
Assignee: |
DAIS ANALYTIC CORPORATION
Odessa
FL
|
Prior
Publication: |
|
Document Identifier |
Publication Date |
|
US 20130165538 A1 |
June 27, 2013 |
|
|
Family ID: |
44306164 |
Appl. No.: |
13/521105 |
Filed: |
January 7, 2011 |
PCT Filed: |
January 7, 2011 |
PCT NO: |
PCT/US2011/020502 PCKC 00 |
371 Date: |
November 8, 2012 |
Related U.S. Patent Documents
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Application
Number |
Filing Date |
Patent Number |
|
|
61293637 |
Jan 9, 2010 |
|
|
|
Current U.S.
Class: |
521/27 |
Current CPC
Class: |
Y02E 60/50 20130101;
C08J 2325/08 20130101; C08J 5/2243 20130101; B01J 41/00 20130101;
H01M 2/16 20130101; Y02E 60/10 20130101; H01M 8/1067 20130101; H01B
1/122 20130101 |
Class at
Publication: |
521/27 |
International
Class: |
B01J 41/00 20060101
B01J041/00 |
Claims
1. A membrane having a first major surface and a second major
surface and comprising one or more anionic exchange electrolyte
polymers; wherein the one or more anionic exchange electrolyte
polymers comprise at least a first contiguous domain and a second
contiguous domain that are phase separated; wherein the first
contiguous domain comprises a plurality of repeat units having
moieties with electrostatically bound negative ions and covalently
bound positive ions; wherein the second contiguous domain comprises
a plurality of repeat units with non-charge bearing moieties; and
wherein at least a portion of the contiguous domains extend from
the first major surface of the membrane to the second major surface
of the membrane.
2. The membrane of claim 1 wherein the second contiguous domain
forms an elastic matrix that supports the first contiguous
domain.
3. The membrane of claim 1 wherein the second contiguous domain is
plastic, rubbery, or semi-crystalline.
4. The membrane of claim 1 wherein the membrane forms a permeable
barrier that selectively allows molecules and/or ions that are
soluble in the first contiguous domain to pass between the first
and second major surfaces of the membrane.
5. The membrane of claim 1 wherein the membrane forms a permeable
barrier that selectively allows molecules that have large dipole
moments or that can be dissolved in solvents that have large dipole
moments to pass between the first and second major surfaces of the
membrane.
6. The membrane of claim 5 wherein the solubility of the large
dipole moment molecules in the first contiguous domain is greater
than 10 times the solubility in the first contiguous domain of low
dipole moment molecules that do not pass between the first and
second major surfaces of the membrane.
7. The membrane of claim 1 wherein the membrane has high
permittivity when exposed to DC or slowly varying AC voltages.
8. The membrane of claim 1 wherein the permittivity is at least
50.
9. The membrane of claim 1 wherein the permittivity is at least
1000.
10. The membrane of claim 1 wherein the permittivity is at least
10,000.
11. A method for selectively mass transporting molecules and/or
ions, the method comprising: providing a membrane according to
claim 1 having molecules and/or ions in contact or in close
proximity with the first major surface of the membrane; and
allowing the molecules and/or ions that are soluble in the first
contiguous domain to pass between the first and second major
surfaces of the membrane.
Description
[0001] This application claims the benefit of U.S. Provisional
Application No. 61/293,637, filed Jan. 9, 2010, which is
incorporated herein by reference in its entiretly.
BACKGROUND
[0002] Permeable membranes have been used in a variety of
applications that may require selective mass transport of
molecules. Such applications include, for example, heating,
ventilation, and air conditioning (HVAC) applications; gas
conditioning; desiccation; distillation, desalination, fluid
separation, and purification. However, the utility and/or
efficiency of such applications is frequently limited by the
properties of such permeable membranes and/or problems encountered
in the use of such permeable membranes.
[0003] There is a continuing need for porous membranes with
properties that can allow for efficient and reliable use in a wide
variety of applications.
SUMMARY
[0004] In one aspect, the present disclosure provides a membrane
having a first major surface and a second major surface and
including one or more anionic exchange electrolyte polymers. The
one or more anionic exchange electrolyte polymers include at least
a first contiguous domain and a second contiguous domain that are
phase separated. The first contiguous domain includes a plurality
of repeat units having moieties with electrostatically bound
negative ions and covalently bound positive ions. The second
contiguous domain includes a plurality of repeat units with
non-charge bearing moieties. At least a portion of the contiguous
domains extend from the first major surface of the membrane to the
second major surface of the membrane. In certain embodiments, the
second contiguous domain forms an elastic matrix that supports the
first contiguous domain. In certain embodiments, the second
contiguous domain is plastic, rubbery, or semi-crystalline.
[0005] In certain embodiments, the membrane forms a permeable
barrier that selectively allows molecules and/or ions that are
soluble in the first contiguous domain to pass between the first
and second major surfaces of the membrane. In certain embodiments,
molecules molecules that have large dipole moments or that can be
dissolved in solvents that have large dipole moments can pass
between the first and second major surfaces of the membrane. In
some embodiments, the solubility of such large dipole moment
molecules in the first contiguous domain is greater than 10 times
the solubility in the first contiguous domain of low dipole moment
molecules that do not pass between the first and second major
surfaces of the membrane.
[0006] In certain embodiments, the membrane has high permittivity
when exposed to DC or slowly varying AC voltages. In some
embodiments, the membrane has a permittivity of at least 50, in
other embodiments at least 1000, and in even other embodiments at
least 10,000.
[0007] In another aspect, the present disclosure provides methods
for selectively mass transporting molecules and/or ions. In some
embodiments, the method includes: providing a membrane as described
herein having molecules and/or ions in contact or in close
proximity with a first major surface of the membrane; and allowing
the molecules and/or ions that are soluble in the first contiguous
domain to pass between the first and second major surfaces of the
membrane.
[0008] Selectively permeable and ion-conducting anionic exchange
electrolyte membranes that include statistical, random, or block
copolymers that have self assembled through phase separation to
form contiguous domains from the first surface of the membrane to
the second surface of the membrane are disclosed herein. The phase
separation can give these modified polymers superior ion transport,
water mass transport, and other electrical properties useful in
many applications. Such applications include water-conducting
membranes for humidification of gases in chemical processes,
electrochemical processes, water conducting membranes for heat and
moisture exchange in heating/ventilation/air conditioning systems,
and ion conducting membranes for the production and storage of
electricity in fuels cells, batteries, and capacitors.
[0009] As used herein, "a," "an," "the," and "at least one" are
used interchangeably and mean one or more than one.
[0010] As used herein, the term "comprising," which is synonymous
with "including" or "containing," is inclusive, open-ended, and
does not exclude additional unrecited elements or method steps.
[0011] The above brief description of various embodiments of the
present disclosure is not intended to describe each embodiment or
every implementation of the present disclosure. Rather, a more
complete understanding of the disclosure will become apparent and
appreciated by reference to the following description and claims in
view of the accompanying drawing. Further, it is to be understood
that other embodiments may be utilized and structural changes may
be made without departing from the scope of the present
disclosure.
BRIEF DESCRIPTION OF THE DRAWINGS
[0012] FIG. 1 is a schematic illustration of an exemplary membrane
cross section showing charge domains and ion and/or moisture
conducting paths from a first surface of the membrane to a second
surface of the membrane.
[0013] FIG. 2 is a transmission electron micrograph (TEM) of an
exemplary ionomeric membrane showing nano-structure with 30
micrometer dark channels at 10.sup.5.times. magnification.
[0014] FIG. 3 is a schematic illustration of an exemplary process
to convert a polymer to an anionic exchange electrolyte.
[0015] FIG. 4 is a reproduction of a nuclear magnetic resonance
(NMR) spectrum of the exemplary chloromethylated ESI polymer
obtained in Example 1.
[0016] FIG. 5 is a reproduction of a nuclear magnetic resonance
(NMR) spectrum of an exemplary CM-SBS obtained in Example 2.
DETAILED DESCRIPTION OF ILLUSTRATIVE EMBODIMENTS
[0017] In one aspect, the present disclosure relates to a membrane
including a plurality of acid-stable and or base-stable polymer
molecules each having at least one ion and mass conducting
component covalently bonded to at least one flexible, plastic or
rubbery or semi-crystalline connecting component. The membrane has
ion and mass conducting components of the polymer molecules ordered
such that a plurality of continuous ion and or mass conducting
channels penetrates the membrane from a first surface to a second
surface and such that the ion and mass conducting channels are
situated in an elastic matrix formed by the flexible, plastic or
rubbery or semi-crystalline connecting components. (See FIG. 1).
Optimally, the channels have a cross-sectional dimension in the
plane of the membrane of about 0.01 micormeter to 0.1 micrometer.
(See FIG. 2).
[0018] The ion and mass conducting component may contain a moiety
consisting of a covalently bound positive ion and an
electrostatically bound negative ion. The polymer containing both
the ion and mass conducting component and the elastic matrix formed
by the flexible, plastic or rubbery or semi-crystalline connecting
component forms an ionomeric polymer molecule also known as an
anionic exchange electrolyte. The membrane formed from ionomeric
polymer molecule includes a selective transfer membrane having a
first surface and a second surface with the ability to transfer
molecules which are soluble in the ion and mass conducting domains
from the first surface to the second surface. The ionomeric polymer
domains of the selective transfer membrane may form contiguous
conduits suitable to provide for travel of high-dipole liquids or
gases between the surfaces of the membrane. Additionally, the
ionomeric polymer has a base resin and the base resin before
ionomerization of the ionomeric polymer is selected from the group
consisting of: polyethylene (PE), polypropylene (PP), polyethylene
oxide (PEO), polystyrene (PS), polyesters, polycarbonate (PC),
polyvinyl chloride (PVC), nylon, halogenated polymers or copolymers
such as perfluorinated copolymers, poly(methyl methacrylate)
(PMMA), acrylonitrile butadiene styrene (ABS), polyamide (PA),
polytetrafluoroethylene (PTFE) (such as Gore-Tex.RTM.), polylactic
acid (PLA), polyvinylidene chloride (PVDC), styrene-butadiene
rubber (SBR), styrene-ethylene/butylenes-styrene (SEBS);
styrene-ethylene/propylene-styrene (SEPS), ethylene-styrene
interpolymer (ESI), styrene acrylate, polyetherether ketone (PEEK),
polyethylene terephthalate (PET or PETE), polybenzimidazole (PM),
phosphoric acid based membranes, Nafion.RTM. (sulfonated
tetrafluorethylene copolymer), and any combination thereof.
[0019] As disclosed herein, the selective transfer membrane can
include a barrier layer including a polymer or polymer composite
that is permeable to high dipole moment material. In certain
instances, the membrane assembly includes a selective transfer
membrane having a first surface and a second surface and further
including a porous support having a first surface and a second
surface, the second surface of the selective transfer membrane
being positioned adjacent to the first surface of the porous
support, the first surface of the membrane assembly being the first
surface of the selective transfer membrane and the second surface
of the membrane assembly being the second surface of the porous
support, which may be hydrophilic.
[0020] As used herein, the term "polymer" includes, but is not
limited to homopolymers, copolymers, such as for example, block,
graft, random and alternating copolymers, terpolymers, etc. and
blends and modification thereof. In addition, unless otherwise
specifically limited, the term "polymer" also includes all possible
geometric configuration of the molecule including, but not limited
to, isotactic, synthdiotactic, atactic and random symmetries.
Further, the term "polymer" includes, but is not limited to
hydrocarbon polymer and fluoropolymer.
[0021] In the polymer, suitable aromatic vinyl monomer which may be
employed according to the present disclosure include styrene as
well as .alpha.-methyl styrene, the lower alkyl or phenyl-ring
substituted derivatives of styrene, such as ortho-, meta-, and
para-methylstyrene, or mixtures thereof, and ring halogenated
styrene, vinyl benzocyclobutanes and divinylbenzene.
[0022] In the polymer, aromatic vinyl monomers and olefins the
monomers are preferably combined in a proportion so as to achieve
aromatic vinyl monomer content of at least 1.0 mole percent in the
resulting polymer more preferably from 1.5 to less than 95 mole
percent, highly preferably 5 to 65 mole percent, and most
preferably from more than 8 up to 64 more percent.
[0023] A block copolymer which has, as it constituents, a polymer
block (A) having as a unit an aromatic vinyl monomer such as
styrene, .alpha.-methyl styrene, styrene whose hydrogen atom bonded
to the benzene ring can be replaced with 1 to 4 alkyl groups
(methyl, ethyl, n-propyl and isopropyl, n-butyl, isobutyl,
tert-butyl groups, etc.), vinylnaphthalene, vinylanthracene,
vinylpyrene, vinyl pyridine, etc.; and has anion-conducting groups
on the polymer block (A), and a flexible polymer block (B) having
as a unit olefin is composed of alkene units, conjugated diene
units or the like. Both Polymer block (A) or (3) can contain one or
plural other monomer units so long as they do not unduly effect the
properties of the polymer, such monomers include, for example,
(meth)acrylic ester ((methyl(meth)acrylate, ethyl(meth)acrylate,
butyl(meth)acrylate, etc); vinyl esters (vinyl acetate, vinyl
propionate, vinyl butyrate, vinyl pivalate, etc.); vinyl ether
(methyl vinyl ether, isobutyl vinyl ether, etc.). These can be used
alone or in a combination of two or more. When two or more are
copolymerized, the form thereof can be random copolymerization,
block copolymerization, graft copolymerization, and/or tapered
copolymerization.
[0024] The polymer may be blended with synthetic polymer to provide
blends have desirable properties. In particular, polyethylene,
ethylene/.alpha.-olefin copolymers, polypropylene, polystyrene,
styrene/acrylonitrile copolymer (including rubber modified
derivatives thereof), syndiotactic polystyrene, polycarbonate,
polyamide, aromatic polyester, polyisocyanate, polyurethane,
polyacrylonitrile, silicone, and polyphenyloxide polymer.
[0025] The anionic exchange polymer electrolyte layer includes a
polymer having a plurality of chemically bound positive ions and a
plurality of electrostatically bound negative ions. A wide variety
of anionic exchange polymer electrolytes can be used in the
devices, methods, and systems disclosed herein. Exemplary
chemically bound positive ions include ammonium (e.g., quaternary
ammonium), phosphonium (e.g., quatemary phosphonium), sulfonium
(e.g., tertiary sulfonium), and combinations thereof. Exemplary
electrostatically bound negative ions include, for example, halides
(e.g., chloride, fluoride, bromide, and/or iodide), pseudohalides
(e.g., azides, isocyanides), SbF6.sup.-, PF6.sup.-, and
combinations thereof. In certain embodiments, the anionic exchange
polymer electrolyte layer can include an optionally crosslinked
anionic exchange polymer (e.g., an iodide anionic exchange
polymer).
[0026] In certain embodiments, the anionic exchange polymer
electrolyte can be a polystyrene having
--CH.sub.2NR.sub.3.sup.+X.sup.- groups attached to the aromatic
ring (e.g., in the ortho and/or para positions) of at least a
portion of the styrene units, wherein each R can independently
represent a C1-C10 alkyl group, and X can represent a halide. A
particularly preferred anionic exchange polymer electrolyte can be
a polystyrene having --CH.sub.2N(CH.sub.3).sub.3.sup.+I.sup.-
groups attached to the aromatic ring of at least a portion of the
styrene units, which can conveniently be prepared by aminating a
chloromethylated polystyrene with a tertiary amine, and exchanging
chloride for iodide.
[0027] In general, ionomers contain both polar and non-polar
moieties, which may each group together. The polar ionic moieties
tend to cluster together and separate from the nonpolar backbone
moieties, which allows for thermoplasticity, especially when
heated. This increased thermoplasticity can allow for increased
energy storage and increased ability to cycle. Additionally, the
non-ionic areas can exhibit adhesive properties. In certain
embodiments, a balance between thermoplasticity and flow at a
certain temperature can be desirable.
[0028] In certain embodiments, the anionic exchange polymer
electrolytes can include, for example, arene-containing linear side
chains, non-arene-containing linear side chains, saturated linear
side chains, unsaturated linear side chains, and flexible
hydrocarbon linear side chains. In certain embodiments, the anionic
and/or cationic exchange polymer electrolytes can be, for example,
unsubstituted and/or substituted (e.g., substituted with
heteroatoms such as oxygen, nitrogen, or other non-carbon atoms).
In certain embodiments, the anionic and/or cationic exchange
polymer electrolytes can are capable of being dissolved in
chlorinated solvents, and may stay in solution at cold
temperatures.
[0029] As used herein, an "alkene moiety" refers to a hydrocarbon
chain containing at least one carbon-carbon double bond. An "arene
moiety" refers to a monovalent or divalent aryl or heteroaryl
group. An aryl group refers to hydrocarbon ring system including
hydrogen, 6 to 18 carbon atoms, and at least one aromatic ring. The
aryl group may be a monocyclic or polycyclic (e.g., bicyclic,
tricyclic, or tetracyclic) ring system, which may include fused or
bridged ring systems. Aryl groups include, but are not limited to,
aryl groups derived from aceanthrylene, acenaphthylene,
acephenanthrylene, anthracene, azulene, benzene, chrysene,
fluoranthene, fluorene, as-indacene, s-indacene, indane, indene,
naphthalene, phenalene, phenanthrene, pyrene, and triphenylene.
Preferably, an aryl group is derived from benzene. A heteroaryl
group refers to a 5 to 14 membered ring system including hydrogen
atoms, one to thirteen carbon atoms, one to six heteroatoms (e.g.,
nitrogen, oxygen, and/or sulfur), and at least one aromatic ring.
The heteroaryl group may be a monocyclic or polycyclic (e.g.,
bicyclic, tricyclic, or tetracyclic) ring system, which may include
fused or bridged ring systems. The nitrogen, carbon, and/or sulfur
atoms in the heteroaryl radical may optionally be oxidized, and the
nitrogen atom may optionally be quatemized. Examples include, but
are not limited to, azepinyl, acridinyl, benzimidazolyl,
benzindolyl, 1,3-benzodioxolyl, benzofuranyl, benzooxazolyl,
benzothiazolyl, benzothiadiazolyl, benzo[b][1,4]dioxepinyl,
benzo[b][1,4]oxazinyl, 1,4-benzodioxanyl, benzonaphthofuranyl,
benzoxazolyl, benzodioxolyl, benzodioxinyl, benzopyranyl,
benzopyranonyl, benzofuranyl, benzofuranonyl, benzothienyl
(benzothiophenyl), benzothieno[3,2-d]pyrimidinyl, benzotriazolyl,
benzo[4,6]imidazo[1,2-a]pyridinyl, carbazolyl, cinnolinyl,
cyclopenta[d]pyrimidinyl,
6,7-dihydro-5H-cyclopenta[4,5]thieno[2,3-d]pyrimidinyl,
5,6-dihydrobenzo[h]quinazolinyl, 5,6-dihydrobenzo[h]cinnolinyl,
6,7-dihydro-5H-benzo[6,7]cyclohepta[1,2-c]pyridazinyl,
dibenzofuranyl, dibenzothiophenyl, furanyl, furanonyl,
furo[3,2-c]pyridinyl,
5,6,7,8,9,10-hexahydrocycloocta[d]pyrimidinyl,
5,6,7,8,9,10-hexahydrocycloocta[d]pyridazinyl,
5,6,7,8,9,10-hexahydrocycloocta[d]pyridinyl, isothiazolyl,
imidazolyl, indazolyl, indolyl, indazolyl, isoindolyl, indolinyl,
isoindolinyl, isoquinolyl, indolizinyl, isoxazolyl,
5,8-methano-5,6,7,8-tetrahydroquinazolinyl, naphthyl,
naphthyridinyl, 1,6-naphthyridinonyl, oxadiazolyl, 2-oxoazepinyl,
oxazolyl, oxiranyl,
5,6,6a,7,8,9,10,10a-octahydrobenzo[h]quinazolinyl,
1-phenyl-1H-pyrrolyl, phenazinyl, phenothiazinyl, phenoxazinyl,
phthalazinyl, pteridinyl, purinyl, pyrrolyl, pyrazolyl,
pyrazolo[3,4-d]pyrimidinyl, pyridinyl, pyrido[3,2-d]pyrimidinyl,
pyrido[3,4-d]pyrimidinyl, pyrazinyl, pyrimidinyl, pyridazinyl,
pyrrolyl, quinazolinyl, quinoxalinyl, quinolinyl, quinuclidinyl,
isoquinolinyl, tetrahydroquinolinyl,
5,6,7,8-tetrahydroquinazolinyl,
5,6,7,8-tetrahydrobenzo[4,5]thieno[2,3-d]pyrimidinyl,
tetrahydro-5H-cyclohepta[4,5]thieno[2,3-d]pyrimidinyl,
5,6,7,8-tetrahydropyrido[4,5-c]pyridazinyl, thiazolyl,
thiadiazolyl, triazolyl, tetrazolyl, triazinyl,
thieno[2,3-d]pyrimidinyl, thieno[3,2-d]pyrimidinyl,
thieno[2,3-c]pridinyl, and thiophenyl (i.e. thienyl).
[0030] As used herein, an "arene-containing linear side chain"
refers to an unbranched hydrocarbon chain consisting only of carbon
and/or hydrogen, wherein at least one carbon in the chain is
replaced with an aryl or heteroaryl group, as defined above.
[0031] As used herein, a "non-arene-containing linear side chain"
refers to an unbranched hydrocarbon chain consisting only of carbon
and/or hydrogen and containing no aryl or heteroaryl groups within
the chain.
[0032] As used herein, an "unsaturated linear side chain" refers to
an unbranched hydrocarbon chain consisting only of carbon and/or
hydrogen and including at least one carbon-carbon double bond or at
least one carbon-carbon triple bond. As used herein, a "saturated
linear side chain" refers to an unbranched hydrocarbon chain
consisting only of carbon and/or hydrogen and containing no
carbon-carbon double bonds and no carbon-carbon triple bonds.
[0033] As used herein, a "flexible hydrocarbon linear side chain"
refers to a flexible connecting component as disclosed, for
example, in U.S. Pat. No. 5,468,574 (Ehrenberg et al.) and U.S.
Pat. No. 5,679,482 (Ehrenberg et al.).
[0034] Various types of copolymers, including block copolymers,
exist that may be used with certain embodiments disclosed herein.
For example, alternating copolymers include regular alternating A
and B chemical or constitutional units; periodic copolymers contain
A and B units arranged in a repeating sequence (e.g.,
(A-B-A-B-B-A-A-A-B-B)n); random copolymers including random
sequences of monomer A and monomer B units; statistical copolymers
including an ordering of distinct monomers within the polymer
sequence that obeys statistical rules; block copolymers that
include two or more homopolymer subunits linked by covalent bonds
such as, for example, diblock, tri-block, tetra-block or other
multi-block copolymers. See, for example, IUPAC, Pure Appl Chem
(1996) 68:2287-2311.
[0035] Additionally, any of the copolymers described may be linear
(including a single main chain), or branched (including a single
main chain with one or more polymeric side chains) Branched
copolymers that have side chains that are structurally distinct
from the main chain are known as graft copolymers. Individual
chains of a graft copolymer may be homopolymers or copolymers, and
different copolymer sequencing is sufficient to define a structural
difference. For example, an A-B diblock copolymer with A-B
alternating copolymer side chains is considered a graft copolymer.
Other types of branched copolymers include star, brush, and comb
copolymers. Any one of these copolymers, or any mixture thereof,
may be utilized with certain aspects of the disclosed devices.
[0036] In certain embodiments, the anionic exchange polymer
electrolytes can include, for example, a polymer including at least
one block. In certain embodiments, the polymer is a thermoplastic
block copolymer. In other embodiments, the polymer is a block
copolymer that includes differentiable monomeric units. Preferably,
at least one of the monomeric units of the block copolymer includes
an arene moiety-containing unit: In other preferred embodiments, at
least one block includes a non-arene moiety-containing unit. In
certain embodiments, the block copolymer includes at least two
monomeric units arranged in statistically random order. In other
embodiments, the block copolymer includes at least two monomeric
units arranged in ordered sequence. In certain embodiments, the
anionic and/or cationic exchange polymer electrolytes can include,
for example, not only polymers or block copolymers, but also
copolymers with other ethylenically unsaturated monomers (e.g.,
acrylonitrile, butadiene, methyl methacrylate, and combinations
thereof).
[0037] In certain embodiments, a block copolymer can be a block
copolymer having at least a first block of one or more mono
alkene-arene moieties, such as styrene, ring-substituted styrene,
.alpha.-substituted styrene, or any combination thereof; and a
second block of a controlled distribution copolymer of a diene
moiety and a mono alkene-arene moiety. The block copolymer can be
any configuration of "A" and "B" blocks, and such block copolymers
can be generated by a wide variety of methods known to one of skill
in the art.
[0038] As used herein, a "mono alkene-arene moiety" refers to one
or more alkene . moieties, as defined above, covalently bonded to
an arene moiety, as defined above. An example of a "mono
alkene-arene moiety" is styrene. A "poly alkene-arene moiety"
refers to a two or more mono alkene-arene moieties, as defined
above, covalently bonded to each other to form a chain including
two or more mono alkene-arene moieties. An example of a "poly
alkene-arene moiety" is polystyrene. A "diene moiety" refers to a
hydrocarbon chain containing two carbon-carbon double bonds. In
certain embodiments, the diene moiety may be conjugated,
unconjugated, or cumulated.
[0039] Some specific examples of block copolymers include, for
example, those described in U.S. Pat. No. 4,248,821 (Van Dellen),
U.S. Pat. No. 5,239,010 (Balas et al.), U.S. Pat. No. 6,699,941
(Handlin et al.), U.S. Pat. No. 7,001,950 (Handlin, Jr. et al.),
U.S. Pat. No. 7,067,589 (Bening et al.), U.S. Pat. No. 7,169,848
(Bening et al.), U.S. Pat. No. 7,169,850 (Handlin, Jr. et al.), and
U.S. Pat. No. 7,186,779 (Joly et al.), and U.S. Patent Application
Publication Nos. 2005/0154144 (Atwood et al.), 2007/0004830 (Flood
et al.), 2007/0020473 (Umana et al.), 2007/0021569 (Willis et al.),
2007/0026251 (Umana), 2007/0037927 (Yang), and 2007/0055015 (Flood
et al.).
[0040] In certain embodiments, the anionic exchange polymer
electrolytes can include, for example, a statistical copolymer. A
statistical copolymer is used herein consistent with the commonly
understood usage in the art. See, for example, Odian, Principles of
Polymerization, 1991. Statistical copolymers can be derived from
the simultaneous polymerization of two monomers and can have, for
example, a distribution of the two monomeric units along the
copolymer chain, which follows Bernoullian (zero-order Markov), or
first or second order Markov statistics. The polymerization may be
initiated by free radical, anionic, cationic, or coordinatively
unsaturated (e.g., Ziegler-Natta catalysts) species. According to
Ring et al., (Pure Appl Chem (1985) 57:1427), statistical
copolymers can be the result of elementary processes leading to the
formation of a statistical sequence of monomeric units that do not
necessarily proceed with equal probability.
[0041] These processes can lead to various types of sequence
distributions including those in which the arrangement of monomeric
units tends toward alternation, tends toward clustering of like
units, or exhibits no ordering tendency at all. Bernoullian
statistics is essentially the statistics of coin tossing;
copolymers formed via Bernoullian processes have the two monomers
distributed randomly and are referred to as random polymers. For
example, it is possible in a free radical copolymerization for the
active end, in the case of one embodiment, a styryl or butadienyl
radical, to have essentially no selectivity for styrene vs.
butadiene. If so, the statistics will be Bemoullian, and the
copolymer obtained will be random. More often than not, there will
be a tendency for the propagating chain end to have some
selectivity for one monomer or the other. In some cases block
copolymers can be derived from the simultaneous copolymerization of
two monomers when the preference of the propagating chain ends for
adding the opposite monomers is very low. The resulting polymer
would be categorized as a block copolymer for the purposes of the
present disclosure.
[0042] Statistical copolymers generally display a single glass
transition temperature. Block and graft copolymers typically
display multiple glass transitions, due to the presence of multiple
phases. Statistical copolymers are, therefore, distinguishable from
block and graft copolymers on this basis. The single glass
transition temperature reflects homogeneity at the molecular level.
An additional consequence of this homogeneity is that statistical
copolymers, such as those of styrene and butadiene, when viewed by
electron microscopy, display a single phase morphology with no
microphase separation. By contrast, block and graft copolymers of
styrene/butadiene, for example, are characterized by two glass
transition temperatures and separation into styrene-rich domains
and butadiene-rich domains. It should be noted that membranes which
are produced from statistical copolymers originally having a single
glass transition temperature and a single phase morphology do not
necessarily exhibit a single phase morphology or a single glass
transition temperature after sulfonation because of chemical
changes in the polymer effected by the sulfonation, in combination
with the physical changes effected by the casting processes of the
present disclosure.
[0043] Pseudo-random copolymers are a subclass of statistical
copolymers which result from a weighted change in the monomer
incorporation that skews the distribution from a random arrangement
(i.e. Bemoullian) that is defined as statistical. Linear
arrangements have been described here, but branched or grafted
including star arrangements of monomers are possible as well. In
addition, block copolymers of styrene and hydrogenated butadiene,
isoprene, or equivalent olefin can be employed. The block
architecture can be monomeric units including diblock, triblock,
graft-block, multi-arm starblock, multiblock, segmented, tapered
block; or any combination thereof.
[0044] In certain such embodiments, the polymer includes moieties
or segments including unsaturated carbon-carbon double bonds, which
are able to be sulfonated. Some examples of such polymers include,
but are not limited to, polybutadiene and/or polyisoprene.
[0045] The weight of the polymers utilized in the present
disclosure are preferably at least approximately 1 kilo Dalton
(KD), 2 KD, 5 KD, 10 KD, 15 KD, 20 KD, 25 KD, 30 KD, 40 KD, 50 KD,
60 KD, 70 KD, 80 KD, 90 KD, or any value therebetween or
greater.
[0046] Some examples of polymers or blocks of polymers that may be
included in certain embodiments include, but are not limited to,
polyethylene (PE), polypropylene (PP), polyethylene oxide (PEO),
polystyrene (PS), polyesters, polycarbonate (PC), polyvinyl
chloride (PVC), nylon, halogenated polymers or copolymers such as
perfluorinated copolymers, poly(methyl methacrylate) (PMMA),
acrylonitrile butadiene styrene (ABS), polyamide (PA), polyurethane
(PU), polytetrafluoroethylene (PTFE), polylactic acid (PLA),
polyvinylidene chloride (PVDC), styrene-butadiene rubber (SBR),
styrene-ethylene/butylenes-styrene (SEBS);
styrene-ethylene/propylene-styrene (SEPS), ethylene-styrene
interpolymer (ESI), styrene acrylate, polyetherether ketone (PEEK),
polyethylene terephthalate (PET or PETE), and any combination of
these or others.
[0047] Polymers of various degrees of polymerization are also
included in the present disclosure. As one of skill in the art
would readily appreciate, the degree of polymerization generally
refers to the number of repeat units or segments in an average
polymer chain at a particular time in a polymerization reaction,
where length is measured by monomer segments or units. Preferable
lengths include, but are not limited to, approximately 500 monomer
units, 1000 monomer units, 5000 monomer units, 10,000 monomer
units, 25,000 monomer units, 50,000 monomer units, 100,000 monomer
units, 200,000 monomer units, 300,000 monomer units, 500,000
monomer units, 700,000 monomer units, or greater or any value there
between.
[0048] The degree of polymerization may also be a measure of the
molecular weight of a polymer. Thus, the degree of polymerization
is equal to the total molecular weight of the polymer divided by
the total molecular weight of the repeating unit or segment.
Polymers with different total molecular weights but identical
composition may exhibit different physical properties. Generally, a
greater degree of polymerization correlates with a greater melting
temperature and greater mechanical strength.
[0049] In certain embodiments, the polymer can include a multiphase
large molecular chain polymer. In some embodiments the multiphase
large molecular chain polymer includes one or more arene-containing
linear side chains, non-arene-containing linear side chains,
saturated linear side chains, unsaturated linear side chains,
and/or flexible hydrocarbon linear side chains.
[0050] In certain embodiments, the exchange polymer electrolytes
can include a wide variety of anion-conducting groups so long as
they are such groups that the material can display sufficient anion
conductivity and moisture transfer properties. Such
anion-conducting groups include an ammonium group optionally
substituted with an alkyl group have 1 to 10 carbon atoms; a
pyridinium group having a methyl group or an ethyl group bonded to
the nitrogen atom or a pyridyl group that has formed a salt with an
acid; an imidazolium group having a methyl group or an ethyl group
bonded to the nitrogen atom or an imidazolyl group that has formed
a salt with an acid; a phosphonium group optionally substituted
with a methyl group or an ethyl group or the like.
[0051] As to the position of introduction of the anion-conducting
groups into polymer block (A), there is no particular restriction,
and they can be introduced either into the aromatic vinyl units or
into other monomer units.
[0052] The amount of the anion-conducting group introduced can be
selected depending upon the application purpose, but usually, in
order to display sufficient ion conductivity for use as a polymer
exchange electrolyte, the amount is preferably sufficient such that
the ion exchange capacity of the block polymer is 0.3 to 4
milliequivalents/g. In certain embodiments, introduction of larger
amounts can result in low mechanical strength and/or low long term
durability.
[0053] Introduction of an anion-conducting group into the resulting
block copolymer can be conducted by a known method. For example,
the obtained block copolymer can be chloromethylated, and then
reacted with an amine or a phosphine. Optionally, the chloride ions
can be replaced with hydroxide ions or other acid anions. A wide
variety of chloromethylation methods known in the art can be used.
For example, a method including adding a chloromethylating agent
and a catalyst into a solution or suspension of the block polymer
in an organic solvent to chloromethylate the block copolymer can be
used. A wide variety of organic solvents including, for example,
halogenated hydrocarbons (e.g., chloroform or dichloroethane) can
be used. Chloromethylating agents including, for example,
chloromethyl ether and/or hydrochloric acid-paraformaldehyde can be
used, and catalysts including, for example, tin chloride and/or
zinc chloride can be used.
[0054] A wide variety of methods for reacting an amine or a
phosphine with a chloromethylated block polymer can be used. For
example, a method including adding an amine or phosphine (e.g., as
a solution in an organic solvent) to a solution or suspension of a
chloromethylated block copolymer in an organic solvent, or a
material formed from the solution or suspension (e.g., a membrane),
can be used. A wide variety of organic solvents can be used for
preparing the solution or suspension including, for example,
methanol, ethanol, acetone, and/or acetonitrile. A wide variety of
amines can be used including, for example, ammonia, primary amines
(e.g., methyl amine), secondary amines (e.g., dimethyl amine), and
combinations thereof can be used to obtain a weakly basic anion
exchange polymer; tertiary amines (e.g., trimethyl amine, triethyl
amine, dimethylethanol amine, methyl diethanol amine, and/or
triethanol amine) can be used to obtain a strongly basic anion
exchange membrane; and diamines or polyamines (e.g., ethylene
diamine or tetramethyl diaminopropane) can be used to obtain an
anion exchange membrane having ion exchange groups bonded to one
another.
[0055] A chloride ion can be introduced as an anion-conducting
group that can optionally be converted to a hydroxide ion or
another acid anion, if desired. A wide variety of methods for
converting the chloride ion to another ion can be used. For
example, a chloride ion can be converted to a hydroxide ion
conducting group by immersing a chloride ion-containing block
copolymer into an aqueous solution of sodium hydroxide or potassium
hydroxide.
[0056] The ion exchange capacity of an anion-conducting copolymer
can be measured using a wide variety of analytical methods known in
the art including, for example, titration methods, infrared
spectroscopic analysis, proton nuclear magnetic resonance (.sup.1H
NMR) spectroscopy, elemental analysis, or combinations thereof.
[0057] In certain embodiments, each layer of electrolyte can have a
lameller nanostructure. For example, certain block copolymers can
self-assemble during the manufacturing process. For example, a
sample of triblock 29 mol % styrene with 55% sulfonation of styrene
blocks was prepared and found to exhibit two Tgs (-40.degree. C.
and 160.degree. C.). The sample was microtomed at -100.degree. C.,
stained with ruthenium tetroxide, and subjected to transmission
electron microscopy (TEM). The micrograph illustrated in FIG. 2
shows lamellae thickness varying from approximately 5 to 30
nanometers. Such structures can have high ionic conductivities, and
can be cross-linked for mechanical stability. The charge density of
such layers can be high, exceeding commercial fluoropolymer
electrolytes by a factor of 2 or 3, as measured by acid
equivalents.
[0058] A multilayer alternating anionic and cationic structure
including unpolarized polymer electrolyte materials as described
herein, can exhibit high permittivity behavior with large frequency
dependence (due to ionic conduction). The multilayer structure was
a four layer alternating anionic and cationic block copolymers of
moderate to low charge density. The anionic and cationic layers had
been heat and pressure fused. No measures were taken to exclude
environmental humidity during the testing. The test equipment was a
parallel plate capacitance with moderate clamping force. A
precision voltage waveform of plus or minus 1 volt with a variable
frequency control of 1/1000 of a hertz to more than a megahertz was
placed across the sample and the input current monitored for phase
delay and distortion. The current phase delay and distortion were
used to calculate the sample capacitance and Tan Delta after
subtracting out the plate and lead capacitances.
[0059] The present disclosure relates to a class of anionic
exchange electrolyte polymers that when formed into membranes have
two sets of related properties. The first is the selective mass
transfer through a solid membrane, which can be useful, for
example, for heating, ventilation, and air conditioning (HVAC), gas
conditioning, desiccation, distillation, desalination, fluid
separation, and purification. The second is the transport of ions
through a solid membrane, which can be useful, for example, in the
production of electricity in devices such as fuel cells and in the
storage of electrical energy in devices such as batteries and
capacitors.
[0060] Anionic exchange electrolyte membranes have been known in
several forms. Each of these membranes can incorporate various
sub-structures and have been typically based around an ammonium
ion. But none of these membranes are known to self assemble into
phases and domains, which can give the membrane superior mechanical
properties and solubility resistance. In addition, these membranes
known in the art have had limited ion conduction capability.
[0061] The acquisition of a desired concentration of a particular
dipole (e.g., high-dipole) moment material from a material
containing the dipole moment material is a common problem faced in
many applications. For example, desalination is the acquisition of
a nearly 100% concentration of a high-dipole moment material,
namely liquid water, from a material, namely salt water (such as
seawater), containing the liquid water. Further, desiccation is the
acquisition of a nearly 0% concentration of a high-dipole moment
material, namely liquid water, from a material, such as moist air,
containing the liquid water.
Selective Permeation
[0062] Similarly, many other applications are concerned with the
acquisition of a desired concentration one or more selected
materials such as dissolved ions, oxides, and the like from a
material containing the one or more selected materials. For
example, CO.sub.2 extraction from flue gas is the acquisition of a
nearly 0% concentration of one or more selected materials, namely
CO.sub.2, from a material, namely flue gas, containing
CO.sub.2.
[0063] A large portion of thermal energy and electrical energy is
devoted to the acquisition of desired concentrations of a
particular material. Therefore, a need exists for efficient systems
and processes for obtaining such concentrations. Even a small
improvement in efficiency may aggregate into a large energy
savings.
Heating and Air Conditioning
[0064] Membranes composed of hydrophilic polymers have been used in
heating, ventilating and air conditioning systems to improve
control of humidity while reducing energy costs. Systems function
by allowing transfer moisture from a humid air stream to a
relatively dry one. One of the functions of a HVAC
(heating/ventilation/air conditioning) system in a building is to
exhaust air to the atmosphere and simultaneously replenish the
exhausted air with fresh air. It may be desired to adjust the
temperature of the fresh air to approximately the same temperature
and humidity of the exhausted air before introducing it into the
building. This can require additional cooling or warming of the
fresh air and the addition or removal of moisture, at a significant
energy cost. In addition, this ventilating process frequently
employs moving parts in the apparatus which may require periodic
maintenance. In order to minimize energy and maintenance costs, it
is desirable to provide a static heat and moisture exchanging core
for simultaneously and continuously effecting both heat and
moisture exchange between two air streams. An inexpensive
water-conducting membrane having mechanical strength is desirable
in order to provide an improved operating lifetime for such cores.
U.S. Pat. No. 4,051,898 to Yoshino discloses the use of Japanese
paper to transfer heat and moisture between fresh intake air and
exhausted room air in an HVAC system. Zhang and Jiang (J. Membrane
Sci., pages 29-38 (1999)) disclose an energy recovery ventilator
wherein heat and water are transferred across a porous hydrophilic
polymer membrane. In U.S. Pat. No. 5,348,691 McElroy et al.
disclose a humidifying device wherein water is transported across a
membrane composed of a perfluorocarbonsulfonic acid polymer or a
polystyrenesulfonic acid. In preferred embodiments, a membrane as
disclosed herein can allow the transfer of water between two gas
streams separated by the membrane.
[0065] The polymer can form at least a portion of a heat exchanger
configured to heat the flow of the first material to the first
temperature, and when the high-dipole moment liquid joins with the
second material, the high-dipole moment liquid transfers thermal
energy to the second material increasing the second temperature,
the system further including: a heat exchanger configured to
transfer at least a portion of the thermal energy transferred to
the second material to a portion of the flow of the first material
before the portion of the flow of the first material contacts the
membrane.
Desalination
[0066] Methods of acquiring potable water from salt water, such as
brackish water, seawater, and the like, include distilling the salt
water through a hydrophobic porous membrane. These membranes are
typically constructed from hydrophobic materials, such as PTFE or
polypropylene that have been formed into a single highly porous
thin layer containing a high density of very small pores. Membranes
constructed in this manner are often referred to as micro-porous
membranes.
[0067] Micro-porous membranes are typically used when thermally
created concentration differences across the membrane allow liquid
water in contact or in close proximity with a first surface of the
membrane to evaporate through the membrane into a colder
environment that is in contact or in close proximity with a second
surface of the membrane. Membrane material surrounding the pores at
the liquid interface on the first surface of the membrane has a low
surface energy and will not allow liquid to enter. Instead, the
surface tension of the water forms a meniscus or "bridge" over the
entrance to these pores. Water molecules transition from a
low-entropy liquid state to a high-entropy vapor state within this
meniscus. The water vapor diffuses into the bulk of the membrane
and transits from the first surface to the second surface of the
membrane, where it comes in contact with the lower temperature
liquid and re-condenses. In this type of membrane, the dissolved
ions in the water are left within the water meniscus covering the
pores at the liquid interface.
[0068] These membranes can experience several failure mechanisms
during use. The liquid meniscus, where the conversion to vapor
occurs, concentrates the dissolved ions. Eventually the dissolved
ion concentration can increase to the point where the dissolved
ions precipitate. These precipitated ions can form a barricade over
the pores curtailing the further conversion of liquid water to
vapor. It can be extremely difficult to re-dissolve these
precipitated ions once they form the barricade. The second failure
mechanism can occur when water vapor condenses within the pores of
the membrane. Once enough liquid water has condensed into the pores
to form a path connecting the first and second surfaces of the
membrane, dissolved ions are free to diffuse into the membrane.
These dissolved ions foul the membrane internally and can be
difficult, if not impossible to remove.
[0069] Existing salt-water desalination plants typically use
reverse osmosis membranes. These membranes can be constructed from
hydrophobic polymers and can have porosity and pore size such that
only water can pass through the membrane leaving behind dissolved
salts and minerals contained in the salt water. Because the
materials used to construct these membranes are hydrophobic, a
pressure differential may be utilized to force the water through
the membrane. Therefore, the salt water is typically pressurized to
force it through the membrane.
[0070] Unfortunately, the pressure can also force contaminants that
would otherwise be too large to pass through the membrane into the
pore structure reducing the efficacy of the membrane. Therefore,
the membrane may require cleaning by periodic back-flushing,
surface scouring, or the like to remove these contaminants. In
order to maintain a desired production rate of desalinated water, a
reverse osmosis plant is typically constructed with at least some
excess capacity to allow for membrane cleaning.
[0071] Such reverse osmosis processes may utilize a considerable
amount of energy to force the water through the membrane. Further,
such plants can be expensive due to the complexity of the piping
utilized to support the pressurized operation in addition to
membrane cleaning that may be required. The reverse osmosis process
can also be considered to be unstable because it can be sensitive
to the type and amount of dissolved ions, organic proteins, and
biota in the salt water.
[0072] Therefore, a need also exists for desalination processes
that are more cost-effective, more robust, and/or less energy
intensive than the reverse osmosis process. High charge density
anionic electrolytes can make these processes possible either by
themselves or in conjunction with cationic electrolytes. When used
in conjunction with cationic electrolytes they can form
zwitterionic structures that have other related anti-fouling
properties.
Energy Storage
[0073] Electrical energy storage devices, such as capacitors,
batteries, and ultracapacitors, store or create energy by utilizing
the electric charge on two metal or otherwise electrically
conductive surfaces ("electrodes"). The charge-bearing surfaces are
typically separated by an electrical insulator, or dielectric. As
charge is placed on the conductive surfaces, an electrical field is
established between the electrodes, resulting in a voltage.
Typically, a capacitor physically separates positive and negative
charges, rather than chemically separating the charges, as is
common in batteries. Batteries typically have limited ability to be
recycled and generally cannot deliver energy as quickly as a
capacitor, or without greater losses than occurs with
capacitors.
[0074] A supercapacitor or ultracapacitor is sometimes called a
double-layer capacitor, as it polarizes an electrolytic solution to
store energy electrostatically. The energy storage mechanism of an
ultracapacitor is highly reversible, which allows for the
ultracapacitor to charge and discharge.
[0075] However, capacitors typically have not been able to match
the energy storage capability of batteries due to the lack of
available materials and structures that can tolerate electric
fields of sufficient strength. There is a need for materials that
tolerate high strength electric fields yet can be polarized to
store energy electrostatically. In preferred embodiments, high
charge density anionic electrolytes can provide that
capability.
[0076] The following examples are offered to further illustrate
various specific embodiments and techniques of the present
disclosure. It should be understood, however, that many variations
and modifications understood by those of ordinary skill in the art
may be made while remaining within the scope of the present
disclosure. Therefore, the scope of the disclosure is not intended
to be limited by the following example.
EXAMPLES
Example 1
Chloromethylation of ESI Polymer (Entry No. SZ-2-027)
[0077] Both types of polystyrene-based copolymers, ESI and SBS,
were provided by DAIS ANALYTICAL Corporation. All chemical reagents
are purchased from Aldrich Company unless otherwise specified.
[0078] A schematic illustration of an exemplary process to convert
a polymer to an anionic exchange electrolyte is shown in FIG.
3.
[0079] The chloromethylation reaction was carried in a 5 L
three-necked round-bottomed flask equipped with a condenser, a
thermometer and a mechanical mixer and under the protection of
nitrogen, unless otherwise specified.
[0080] In this example, 200 g (Wp=Weight of polymer) of ESI
polymers (P=Polymer) were used. The polymers was first completed
dissolved in a solvent mixture containing 1400 mL (V1=Volume of
Reactant 1) of dimethoxymethane DMM, (R1=Reactant 1) under a
temperature not higher than 50.degree. C. to yield a clear polymer
solution. After cooling the polymer solution below the room
temperature, 516 mL (V2=Volume of Reactant 2) of thionyl chloride
(R2=Reactant 2) was added drop-wise in around 10 minutes. The
reaction mixture was then allowed to warm to room temperature and
keep at room temperature for another 45 minutes before was cooled
down again. Then 40 mL (Ac=Amount of Reaction Catalyst) of
ZnCl.sub.2 ethyl ether solutions (Rc=Reaction Catalyst) was added
to the reaction mixture. The reaction mixture was heated to a
designed reaction temperature (Tr) and maintained at this
temperature (Tr) for a period of time (Tt) until the degree of
chloromethylation(Dc) reached the designed value. In this example,
Tr=50.degree. C. and Tt=32 hours were selected.
[0081] After the reaction was completed, the reaction mixture was
poured into 2000 mL of methanol. The precipitates were filtered out
and washed with methanol three times, then dried in air to give the
chloromethylated ESI polymer, CM-ESI. The chloromethylation degree
was estimated from NMR spectra (FIG. 4) and a Dc=37% was obtained
from this example.
Example 2
Chloromethylation of SBS Polymer (Entry No. SZ-2-086)
[0082] In this example, the chloromethylation of SBS polymer was
carried out following the example 1, except that: [0083] P=SBS
Polymer, Wp=150 g [0084] R1=DMM, V1=1327 [0085] R2=Thionyl
chloride, V2=1149 [0086] Rc=ZnCl.sub.2 ethyl ether solutions, Ac=90
ml [0087] Tr=40.degree. C., Tt=24 hours
[0088] This example yielded the choloromerthylated SBS polymer
CM-SBS, with the a degree of chloromethylation (Dc) of 95% as
estimated from the NMR spectra (FIG. 5).
Example 3
Amination of ESI Polymer (Entry No. SZ-2-097)
[0089] The amination reaction (to covert the chloromethylated
polymer to a quaternary salt by alkyl amine) was carried in a
three-necked round-bottomed flask equipped with a condenser, a
thermometer and a magnetic mixer and under the atmosphere, unless
otherwise specified.
[0090] In this example, the cholormethylated polymer CM-ESI , 15 g
(WPa=Weight of the polymer for amination) was first completed
dissolved in a minimum amount of a polar solvent such as DCM, DCE,
choloroform, THF and the similar. Into this polymer solution, 30 mL
(Va=Volume of Ra) of N,N-dimethylethanolamine, DMEOA, (Ra=Reagent
for amination) was dropped into the solution. The reaction mixture
was stirring for 24 h (Tta=Time of amination) at 20.degree. C.
(Ta=Temperature of amiantion). The aminated polymer was
precipitated by methanol and then washed with methanol three times
followed by 1 M HCl and deionized water again The cleaned aminated
polymer was dried in air.
[0091] This aminated polymer may or may not be subjected to further
treatment with another kind of amination regent (Ra2) depending on
the desired amination degree. The amination degree (Da=Degree of
Amination) was determinate by the standard titration method. In
this example, no further treatment was performed, the amiantion
degree was found to be 23%.
Example 4
Amination of SBS Polymer (Entry No. SZ-2-134 and SZ-2-134-TMA)
[0092] In this example, the amination of chloromethylated SBS
polymer CM-SBS, obtained in Example 2, was carried in a similar
procedure as described in Example 3, except that: [0093] Pa=CM-SBS,
obtained in example 2; WPa=103 g; [0094] Ra=N,N-dimethyloctylamine,
DMOA, Va=500 mL; [0095] Ta=40.degree. C., Tta=24 hours
[0096] The obtained sample sz-2-134 (Entry 4-1 in Table 4) was
further treated with another amine to yield sample sz-2-134-TMA
(Entry 4 in Table 4) following the procedure below.
[0097] 100 grams of the obtained animated polymer sz-2-134
(Pa=sz-2-134) was soaked in 800 mL of 25% trimethyl amine (TMA)
aqueous solution (Ra) at room temperature (Ta=20.degree. C.) for 48
hours (Tta=48 hours). Then, the polymer was filtered out from the
TMA solution, and washed in sequence with deionized water, 1 M HCl,
and deionized water, and dried to yield the final animated SBS
polymer. The amination degree of the final polymer obtained in this
example was 78%.
Examples 5-25
[0098] Examples 5-25 listed in Table 1 are chloromethylation of ESI
polymer under different conditions following the procedure of
Example 1.
TABLE-US-00001 TABLE 1 Reaction conditions and chloromethylation
results for ESI polymer V1 (mL) V2 (mL) Ac (mL) Entry Wp R1 = R2 =
Rc = Tr Tt Dc (%) Sr. Run No. (g) DMM SOCl.sub.2 ZnCl.sub.2
(.degree. C.) (hr) (observation) 1 sz-2-027 200 1400 516 40 50 32
37 5 sz-1-136 10 110 18.4 0.4 40 48 14 6 sz-1-151 50 250 92 2.2 40
48 17 7 sz-1-153 50 300 101 4.2 50 24 26.5 8 sz-1-171 10 88.5 76.6
5 20 3 h 2 9 sz-1-171a 5 44.5 38.3 2.5 40 22 80 (gel) 10 sz-1-173
25 175 64.5 10 50 27 69 11 sz-1-176 25 222.5 191.5 12.5 35 3 37 12
sz-1-177 50 350 129 10 50 21 68 (gel) 13 sz-1-178 50 350 129 20 50
26 40 (gel) 14 sz-1-179 5 35 13 2 50 20 22 15 sz-1-180 250 1750 645
50 50 24 14.5 16 sz-1-181 5 35 12.5 2.5 50 3.2 34.5 17 sz-1-185 200
1400 516 80 50 7 15 18 sz-1-186 200 1400 516 100 50 4.4 32.5 19
sz-1-187 200 1400 516 100 50 7 22 20 sz-2-03 200 1400 516 40 50 31
36.5 21 sz-2-07 200 1400 516 40 50 25.5 34 22 sz-2-015 200 1400 516
40 50 26 26 23 sz-2-024 200 1400 616 100 50 34 39 24 sz-2-222 200
5000 R1 = 50 40 48 78 MMC 25 Sz-2-223 200 5000 R1 = 10 Rc = 40 48
71 MMC SnCl2 (MMC = Methoxymethyl Chloride)
Examples 26-30
[0099] Examples 26-30 listed in Table 2 are chloromethylation of
SBS polymer under different conditions following the procedure of
Example 2.
TABLE-US-00002 TABLE 2 Table of Reaction conditions and
chloromethylation results for SBS polymer V1 (mL) V2 (mL) Ac (mL)
Entry Wp (g) R1 = R2 = Rc = Tr Tt Dc Sr. Run No. P = SBS DMM
SOCl.sub.2 ZnCl.sub.2 (.degree. C.) (hr) (%) 2 sz-2-086 150 1327
1149 90 40 24 95 26 sz-2-009 50 440 129 20 50 29 26 27 sz-2-013 20
177 153 10 40 25 99 28 sz-2-017 50 442 383 25 40 6.5 59 29 sz-2-026
50 442 383 25 40 6.5 63 30 sz-2-133 180 1593 1379 90 40 20 98
Examples 31-37
[0100] Examples 31-37 listed in Table 3 are amination of
chloromethylated ESI polymer under different conditions following
the procedure of Example 3.
TABLE-US-00003 TABLE 3 Animation of ESI polymers Entry WPa Va Ta
Tta Da No. Run No. Pa (g) Ra (ml) (.degree. C.) (hours) (%) 3
sz-2-97 SZ-2-27 15 DMEOA 30 20 24 23 31 sz-2-019 SZ-1-186 50 DMOA
100 40 4 17 32 sz-2-020 SZ-1-186 25 DMOA 50 20 24 12 33 sz-2-85
SZ-2-24 25 DMOA 50 88.5 25 9 34 sz-2-87 SZ-2-27 15 DMOA 30 41 26 10
35 sz-2-89 SZ-2-27 15 TMA Gas 20 4 15 36 sz-2-236 sz-2-222 100
TMA-25% 1500 20 24 64 37 Sz-2-224* Sz-2-236 5 Methanol 500 20 24 64
*SZ-2-224 is the 1% (wt/vol) solution of sz-2-236 in methanol
Examples 38-56
[0101] Examples 38-56 listed in Table 4 are amination of
chloromethylated SBS polymer under different conditions following
the procedure of Example 4.
TABLE-US-00004 TABLE 4 Amination of SBS polymer Entry WPa Va Ta Tta
Da No. Run No. Pa (g) Ra (ml) (.degree. C.) (hour) (%) 4-1 sz-2-134
sz-2-133 103 DMOA 500 40 24 4 sz-2-134-TMA sz-2-134 100 TMA 800 20
48 78 38 z-2-022 sz-2-13 16.4 DMOA 50 40 0.25 31 39 sz-2-35 sz-2-26
20 DMOA 62.5 40 24 35 40 sz-2-36 sz-2-22 14 DMOA 50 42 27 45 41
sz-2-74 sz-2-17 1 NH3-33% 4 20 24 4 42 sz-2-75 sz-2-26 2 Pyridine 3
70 5.5 17 43 sz-2-76 sz-2-26 10 DEA 20 60 6.2 11 44 sz-2-79 sz-2-26
10 DMOA 31 70 17 44 45 sz-2-80 sz-2-17 10 DMOA 31 63 21 33 46
sz-2-82 sz-2-17 10 TEOA 20 60 24 28 47 sz-2-83 sz-2-17 10 TMA-gas
50 2 5 48 sz-2-99-1 sz-2-86 0.5 Pyridine 5.8 20 72 34 49 sz-2-99-2
sz-2-86 0.5 TMA-25% 13 20 72 55 50 sz-2-99-3 sz-2-86 0.5 DMOA 7.5
20 72 48 51 sz-2-135 sz-2-086 5 NH3-33% 70 20 48 2 52 sz-2-118-3
sz-2-86 1.1 TEA 13.2 20 96 27 53 sz-2-114 sz-2-86 120 DMOA 500 62
24 44 54 sz-2-128 sz-2-114 100 TMA-25% 336 20 60 50 55 sz-2-118-1
sz-2-114 3 TMA-25% 42 20 96 77 56 sz-2-118-2 sz-2-114 2.2 TEA 23 20
96 52
Examples 57 and 58
[0102] The quatemary amination process such as using different
amine and its concentration, amination temperature and amination
time were investigated. The anion exchange membranes were
characterized by ion exchange capacity, moisture transfer test, and
ionic conductivity.
[0103] Suitable reaction conditions were found to be amination time
or 24-48 hours, and an amination temperature of 35-45.degree.
C.
Example 57
[0104] The chloromethylated SEBS polymer (5 g) was dissolved in 500
ml chloroform at 35-45.degree. C. for 24 hours. The obtained
polymer solution was then filtered though the nylon screen to
remove undissloved gel particles. The final casting solution (3-5
wt %) was obtained by rotary evaporator and cast onto a silicone
release line to form a base membrane (approximately 1 nail
thickness). The prepared base membranes were then functionalized by
quaternary amination in a trimethylamine aqueous solution. The
reaction conditions at this step such as trimethlyamine
concentration, temperature and time were investigated and shown in
the Table 5. After amination the membranes were rinsed with DI
water and then air dried the membrane for characterization as shown
in Table 5.
Example 58
[0105] The chloromethylated SEBS polymer was dissolved in
chloroform first. Then the polymer solution was functionalized by
quaternary amination with slowly adding triethylamine while
agitation. The reaction conditions at this step such as the amount
of triethlyamine used, temperature and time were investigated and
shown in Table 5. After the reaction the obtained polymer solution
was concentrated and then directly using for casting membrane. The
membranes were soaked in DI water for 4-6 hours and then rinsed
with DI water and air dried the membrane for characterization.
[0106] The membranes were characterized by ion exchange capacity,
moisture transfer test, and ionic conductivity. Each property was
measured for three times, respectively, to obtain an average value
that listed in Table 5.
TABLE-US-00005 TABLE 5 Quaternary Amination of Chloromethylated
SEBS Polymer Moisture CMS:TMA transfer Exam CM or TEA Temp Time IEC
(g/10 min I/C No. (mol %) (mmol; mmol) (.degree. C.) (hrs) (meq/g)
at 30.degree. C.) (S/cm2) 1 79 1:5 35-40 24 0.51 0.019 2 79 1:10
40-45 24 0.83 0.035 3 79 1:20 40-45 24 1.24 0.113 4 79 1:1 35-40 24
1.10 0.091 5 79 1:2 35-40 48 1.32 0.114 6 76 1:2 35-40 40 1.03
0.104 7 76 1:3 25 48 0.98 0.077 8 76 1:3 40-45 24 1.12 0.107 9 76
1:0.75 35-40 24 0.19 10 79 1:1 50 24 0.33 0.025 11 79 1:3 35-40 24
1.92 0.129 12 79 1:5 35-40 24 3.25 0.194 0.0099 13 76 1:5 35-40 24
3.07 0.162 14 79 1:5 35-40 48 3.85 0.231 0.0163 15 76 1:10 35-40 24
4.22 0.271 16 76 1:8 35-40 24 3.65 0.224
[0107] The complete disclosures of the patents, patent documents,
and publications cited herein are incorporated by reference in
their entirety as if each were individually incorporated. Various
modifications and alterations to this disclosure will become
apparent to those skilled in the art without departing from the
scope and spirit of this disclosure. It should be understood that
this disclosure is not intended to be unduly limited by the
illustrative embodiments and examples set forth herein and that
such examples and embodiments are presented by way of example only
with the scope of the disclosure intended to be limited only by the
claims set forth herein as follows.
* * * * *