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Claims  |
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We claim:
1. A process for producing a sulfonated polyaniline composition having a
chemical composition of formula I
##STR8##
wherein O.ltoreq.y.ltoreq.1, R.sub.1, R.sub.2, R.sub.3, R.sub.4, R.sub.5
and R.sub.6 are independently selected from the group consisting of H,
SO.sub.3.sup.-, --SO.sub.3 H, --R.sub.7 SO.sub.3.sup.-, --R.sub.7 SO.sub.3
H, --OCH.sub.3, --CH.sub.3, --C.sub.2 H.sub.5, --F, --Cl, --Br, --I,
--NR.sub.7 2, --NHCOR.sub.7, --OH, --O.sup.-, --SR.sub.7, --OR.sub.7,
--OCOR.sub.7, --NO.sub.2, --COOH, --COOR.sub.7, --COR.sub.7, --CHO and
--CN, wherein R.sub.7 is a C.sub.1 -C.sub.8 alkyl, aryl or aralkyl group,
and wherein the fraction of rings containing at least one R.sub.1,
R.sub.2, R.sub.3 or R.sub.4 group being an --SO.sub.3.sup.-, --SO.sub.3 H,
--R.sub.7 SO.sub.3.sup.-, or --R.sub.7 SO.sub.3 H varies from
approximately 20 percent to one hundred percent, comprising reacting the
polyaniline polymer or substituted polyaniline polymer and SO.sub.3 gas.
2. The process according to claim 1 in which the reaction is conducted at a
temperature range of between about room temperature and 100.degree. C.
3. The process according to claim 1 in which the reaction is carried out in
air or inert atmosphere.
4. The process according to claim 1 in which the polyaniline polymer or
substituted polyaniline polymer has a predetermined chain length which is
not reduced in length during the reaction.
5. The process according to claim 1 in which a copolymer of polyaniline and
sulfonated polyaniline is obtained by partially sulfonating the
polyaniline polymer.
6. The process according to claim 5 in which the partial sulfonation of the
polyaniline polymer comprises shortening sulfonation times and/or lowering
sulfonation temperatures.
7. A sulfonated polyaniline composition of formula I, produced according to
the process of claim 1.
8. The composition of claim 7, wherein the composition is a sulfonated
polyaniline film.
9. The composition of claim 7, wherein the composition is an oriented
sulfonated polyaniline film.
10. The composition of claim 7, wherein the composition is a sulfonated
polyaniline film adhered to a substrate.
11. The composition of claim 7, wherein the composition is a sulfonated
polyaniline fiber.
12. The composition of claim 7, wherein the composition is a polyaniline
powder. |
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Claims  |
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Description  |
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BACKGROUND OF THE INVENTION
The present invention relates to processes for the preparation of
self-protonated sulfonic acid-substituted polyaniline compositions and
their derivatives and uses thereof.
Polyaniline is a family of polymers that has been under intensive study
recently because the electronic and optical properties of the polymers can
be modified through variations of either the number of protons, the number
of electrons, or both. The polyaniline polymer can occur in several
general forms including the so-called reduced form (leucoemeraldine base),
possesing the general formula
##STR1##
the partially oxidized so-called emeraldine base form, of the general
formula
##STR2##
and the fully oxidized so-called pernigraniline form, of the general
formula
##STR3##
In practice, polyaniline generally exists as a mixture of the several forms
with a general formula (I) of
##STR4##
When O.ltoreq.y.ltoreq.1, the polyaniline polymers are referred to as
poly(paraphenyleneamineimines) in which the oxidation state of the polymer
continuously increases with decreasing value of y. The fully reduced
poly(paraphenyleneamine) is referred to as leucoemeraldine, having the
repeating units indicated above corresponding to a value of y=1. The fully
oxidized poly(paraphenyleneimine) is referred to as pernigraniline, of
repeat unit shown above corresponds to a value of y=0. The partly oxidized
poly(paraphenyleneimine) with y in the range of greater than or equal to
0.35 and less than or equal to 0.65 is termed emeraldine, though the name
emeraldine is often focused on y equal to or approximately 0.5
composition. Thus, the terms "leucoemeraldine", "emeraldine" and
"pernigraniline" refer to different oxidation states of polyaniline. Each
oxidation state can exist in the form of its base or in its protonated
form (salt) by treatment of the base with an acid.
The use of the terms "protonated" and "partially protonated" herein
includes, but is not limited to, the addition of hydrogen ions to the
polymer by, for example, a protonic acid, such as mineral and/or organic
acids. The use of the terms "protonated" and "partially protonated" herein
also includes pseudoprotonation, wherein there is introduced into the
polymer a cation such as, but not limited to, a metal ion, M.sup.+. For
example, "50%" protonation of emeraldine leads formally to a composition
of the formula
##STR5##
which may be rewritten as
##STR6##
Formally, the degree of protonation may vary from a ratio of [H.sup.+
]/[--N.dbd.]=0 to a ratio of [H.sup.+ ]/[--N.dbd.]=1. Protonation or
partial protonation at the amine (--NH--) sites may also occur.
The electrical and optical properties of the polyaniline polymers vary with
the different oxidation states and the different forms. For example, the
leucoemeraldine base, emeraldine base and pernigraniline base forms of the
polymer are electrically insulating while the emeraldine salt (protonated)
form of the polymer is conductive. Protonation of emeraldine base by
aqueous HCl (1M HCl) to produce the corresponding salt brings about an
increase in electrical conductivity of approximately 10.sup.12 ;
deprotonation occurs reversibly in aqueous base or upon exposure to vapor
of, for example, ammonia. The emeraldine salt form can also be achieved by
electrochemical oxidation of the leucoemeraldine base polymer or
electrochemical reduction of the pernigraniline base polymer in the
presence of an electrolyte of the appropriate pH. The rate of the
electrochemical reversibility is very rapid; solid polyaniline can be
switched between conducting, protonated and nonconducting states at a rate
of approximately 10.sup.5 Hz for electrolytes in solution and even faster
with solid electrolytes. (E. Paul, et al., J. Phys. Chem. 1985, 89,
1441-1447). The rate of electrochemical reversibility is also controlled
by the thickness of the film, thin films exhibiting a faster rate than
thick films. Polyaniline can then be switched from insulating to
conducting form as a function of protonation level (controlled by ion
insertion) and oxidation state (controlled by electrochemical potential).
Thus, in contrast to, for example polypyrrole, polyaniline can be turned
"on" by either a negative or a positive shift of the electrochemical
potential, because polyaniline films are essentially insulating at
sufficiently negative (approximately 0.00 V vs. SCE) or positive (+0.7 V
vs. SCE) electrochemical potentials. Polyaniline can also then be turned
"off" by an opposite shift of the electrochemical potential.
The conductivity of polyaniline is known to span 12 orders of magnitude and
to be sensitive to pH and other chemical parameters. It is well-known that
the resistance of films of both the emeraldine base and 50% protonated
emeraldine hydrochloride polymer decrease by a factor of approximately 3
to 4 when exposed to water vapor. The resistance increases only very
slowly on removing the water vapor under dynamic vacuum. The polyaniline
polymer exhibits conductivities of approximately 1 to 20 Siemens per
centimeter (S/cm) when approximately half of its nitrogen atoms are
protonated. Electrically conductive polyaniline salts, such as fully
protonated emeraldine salt [(--C.sub.6 H.sub.4 --NH--C.sub.6 H.sub.4
--NH.sup.+)--Cl.sup.- ].sub.x, have high conductivity (10.sup.-4 to
10.sup.+2 S/cm) and high dielectric constants (20 to 200) and have a
dielectric loss tangent of from below 10.sup.-3 to approximately 10.sup.1.
Dielectric loss values are obtained in the prior art by, for example,
carbon filled polymers, but these losses are not as large nor as readily
controlled as those observed for polyaniline.
While the preparation of polyaniline polymers and the protonated
derivatives thereof is known in the art, it is novel to prepare sulfonated
polyaniline compositions which are capable of being "self-protonated" or
"self-doped". The use of the terms "self-protonated" and "self-doped"
herein includes, but is not limited to, the reorganization of hydrogen
ions on the polymer i.e., the absence of any counterion not covalently
bonded to the polymer chain. For example, self-doping or self-protonation
of a polyaniline base polymer leads to a polyaniline salt polymer and a
reorganization of the electronic structure which then forms a polaronic
metal. The conductivity of such polaronic metal is independent of external
protonation.
The present invention is related to the invention disclosed in the parent
copending application Ser. No. 07/423,902 filed Oct. 19, 1989 which is
expressly incorporated herein by reference. That application discloses, in
part, the sulfonation of the emeraldine base form of polyaniline in a
solution phase.
SUMMARY OF THE INVENTION
The present invention provides a process for producing a polymeric acid
polymer which is capable of protonating or doping itself to form an
electrically conducting polymer. The sulfonated polyaniline polymer has
faster electronic, electrochemical, chemical, and optical responses and
improved solubility than the parent polymer, polyaniline. The solubility
of the sulfonated polyaniline polymer is increased greatly due to the
presence of the sulfonic group SO.sub.3 H. The sulfonated polyaniline
polymer is easy to dissolve in basic aqueous solutions in which the
polyaniline polymer is insoluble. In addition, due to the electron
withdrawing effects of the SO.sub.3 H group, the sulfonated polyaniline
polymer has improved environmental stability over the polyaniline polymer.
The present invention relates to a gas phase process for producing the
sulfonated polyaniline which comprises reacting the emeraldine base
polyaniline polymer with gaseous SO.sub.3.
The gas phase sulfonation process of the present invention eliminates the
need for a separation process in order to isolate the sulfonated
polyaniline composition from a sulfuric acid solution.
The gas phase sulfonation process also eliminates the need for large
quantities of reagent, such as methanol or acetone, to precipitate the
sulfonated polyaniline composition from a sulfuric acid solution.
The gas phase sulfonation process is versatile and can be utilized to
sulfonate the emeraldine base polyaniline polymer in a variety of forms
such as, for example, a powder, stretched free standing films, films
adhered to a substrate, and fibers.
Through the use of the gas phase sulfonation process, there is less chance
of causing degradation of the emeraldine base polyaniline composition than
through the use of a sulfuric acid solution.
Further, the gas phase sulfonation process is simple, fast and
uncomplicated, thus providing the industry with an attractive alternative
for producing self-protonated conducting sulfonated polyaniline
compositions.
BRIEF DESCRIPTION OF THE DRAWINGS
FIG. 1 is a schematic illustration of the different structures of
sulfonated polyaniline, (a and b), the ammonia salt (c), and the
emeraldine base (d).
FIG. 2 is a schematic diagram of a method of gas phase sulfonation of a
polyaniline composition.
FIG. 3 is a schematic diagram of another method of gas phase sulfonation of
a polyaniline composition.
FIG. 4 is a schematic diagram of another method of gas phase sulfonation of
a polyaniline composition.
DETAILED DESCRIPTION OF THE INVENTION
The present invention relates to a process for the preparation of sulfonic
acid substituted polyaniline compositions, their derivatives and uses
thereof.
The self-protonated sulfonated polyaniline compositions have the formula I
##STR7##
wherein O.ltoreq.y.ltoreq.1; R.sub.1, R.sub.2, R.sub.3, R.sub.4, R.sub.5
and R.sub.6 are independently selected from the group consisting of H,
--SO.sub.3.sup.-, --SO.sub.3 H, --R.sub.7 SO.sub.3.sup.-, --R.sub.7
SO.sub.3 H, --OCH.sub.3, --CH.sub.3, --C.sub.2 H.sub.5, --F, --Cl, --Br,
--I, --NR.sub.7 2, --NHCOR.sub.7, --OH, --O.sup.-, --SR.sub.7, --OR.sub.7,
--OCOR.sub.7, --NO.sub.2, --COOH, --COOR.sub.7, --COR.sub.7, --CHO and
--CN, wherein R.sub.7 is a C.sub.1 -C.sub.8 alkyl, aryl or aralkyl group.
For the sake of clarity, the structure shown in formula I is in the non
self-protonated form.
The fraction of rings containing at least one R.sub.1, R.sub.2, R.sub.3 or
R.sub.4 groups being an --SO.sub.3.sup.-, --SO.sub.3 H, --R.sub.7
SO.sub.3.sup.- or --R.sub.7 SO.sub.3 H can be varied from a few percent to
one hundred percent. In certain embodiments the percentage ranges from at
least approximately 20% up to and including 100%. It is within the
contemplated scope of the present invention that the --R.sub.7
SO.sub.3.sup.- and --R.sub.7 SO.sub.3 H substituents can be varied so that
the sulfonated polyaniline is soluble in a range of solvents in order to
make the sulfonated polyaniline polymer more easily blendable with other
polymers and/or more easily cast onto a variety of surfaces.
The solubility of sulfonated polyaniline can be varied by changing the
degree of sulfonation (i.e., the sulfonation time and/or temperature in
H.sub.2 SO.sub.4 (SO.sub.3)). It is noted that the oxidation state of the
polymer (from leucoemeraldine through emeraldine to pernigraniline) and
the degree of sulfonation (x) can be independently varied. Here x is the
fraction of C.sub.6 rings which have an SO.sub.3.sup.- or SO.sub.3 H group
attached.
When x=0, the polymer does not dissolve in either basic or acidic aqueous
solutions. Upon increasing the value of x, the polymer becomes soluble in
strongly basic, basic, weakly basic and eventually in acidic aqueous
solutions. This progressive improvement in solubility implies that the
polymer becomes soluble in neutral media, particularly H.sub.2 O, at the
appropriate value of x, yielding a water-soluble conducting polymer. The
color of soluble sulfonated polyaniline in acidic solution is green,
indicating it is the conducting salt form.
The solubility of polyaniline is increased greatly in basic aqueous
solution by the presence of --SO.sub.3 H group on the phenyl rings. This
is in contrast with polyaniline which when washed with basic solutions,
converts to the insoluble base form.
Protonation of the emeraldine base polymer leads to the emeraldine salt
polymer and a reorganization of the electronic structure to form a
polaronic metal. Since benzenesulfonic acid is a strong acid, about as
strong as hydrochloric acid, the sulfonated polyaniline is capable of
self-doping. Hence, the conductivity of the sulfonated polyaniline is
independent of external protonation.
Being able to dope itself, the sulfonated polyaniline polymer has enhanced
optical and electrical response to electrochemical potential as compared
with the parent polyaniline polymer. Since the solid-state diffusion of
counterions in and out of a polymer during electrochemical processes is
often the rate controlling step in the kinetics, it also limits the speed
of both optical and electrical response of polymers. In the self-doped
conjugated polymer of the present invention, the counterions are not
necessary from the medium. The positive charge introduced into the
conjugated pi electron system of the backbone of the polymer is
compensated by the protons migrating out of the polymer, or vice versa,
leaving behind the opposite charged counterion. Being the smallest and
most mobile ion, proton hopping mechanisms lead to relatively fast doping
kinetics as compared to those counterions migrating in or out of the
polymer. As a consequence, it is possible to achieve sufficient speed to
be useful for a variety of technological applications.
Without external doping, the sulfonated polyaniline has a conductivity of
0.1 S/cm, which makes the sulfonated polyaniline a self-doped conducting
polymer. The results indicate that the amount of charge injected into or
ejected out of the sulfonated polyaniline polymer is quite similar to that
of polyaniline. Charge transfer doping within a specific potential range
in solutions such as 1.0 M HCl and 0.5M H.sub.2 SO.sub.4 is highly
reversible in the air reflecting the environmental stability introduced by
the sulfonic acid groups. The inventors present the dependence of
positions of redox peaks on different pH values and compare the results
with those of sulfonated polyaniline. In contrast with polyaniline, the
first redox process depends on pH in the value range of -0.2 to about 7
due to the sulfonic acid protons on the sulfonated polyaniline backbones.
The second redox process depends on the pH in a manner similar to that of
polyaniline.
The chemical synthesis of the sulfonated polyaniline polymers of the
present invention is accomplished by reacting polyaniline with
concentrated or fuming sulfuric acid, SO.sub.3 gas or other sulfonation
agents in either air or inert gases. Examples of several of the methods
for such syntheses are disclosed below.
Materials-Aniline and other chemicals were obtained from Aldrich and were
all reagent grade or better. Hydrochloric acid and ammonium hydroxide were
used as received. Different pH buffer solutions were commercially
purchased.
Chemical Synthesis I: Emeraldine hydrochloride powder was synthesized from
aniline and (NH.sub.4)S.sub.2 O.sub.8 then converted to analytically pure
emeraldine base polyaniline using the method described previously in A. G.
MacDiarmid, J. C. Chiang, A. F. Richter, N. L. D. Somasiri and A. J.
Epstein in L. Alcacer (ed.) Conducting Polymers, D. Reidel Publishing Co.,
Dordrecht, The Netherlands (1987).
For the sulfonation of polyaniline, 1.5 g polyaniline (dry emeraldine base
form) was dissolved into 40 ml fuming sulfuric acid H.sub.2 SO.sub.4
(SO.sub.3) with constant stirring at room temperature. During the
sulfonation period the color of the solution changed from dark purple to
dark blue. After approximately 2 hours, the solution was slowly added
during about 20 minutes to 200 ml methanol while maintaining the
temperature between about 10.degree.-20.degree. C. by an ice bath. A green
powder precipitate was formed during the mixing. After the mixing, 100 ml
of less polar acetone was added to the solution in order to increase the
precipitate. The green powder was then collected on a Buchner funnel using
a water aspirator. The precipitate cake was washed portionwise (50
ml/portion) with methanol until the portion of the filtrate showed pH=7
when tested by wet pH paper. The liquid level in the Buchner funnel was
constantly adjusted so that it remained above the top of the precipitate.
This prevented cracking of the precipitate cake, which would result in
inefficient washing of the precipitate cake.
After the above washing, the precipitate remained under suction for
approximately 10 minutes. It was then transferred on the filter paper to a
vacuum desicator and dried under dynamic vacuum for 24 hours. Elemental
analyses, as shown in Table I are consistent with the composition shown in
FIG. 1 as structure a, compound I, which is sulfonated, protonated
polyaniline in the emeraldine oxidative state. The self-doped polyaniline
is readily dissolved in a dilute aqueous base solution to form a
homogeneous blue-violet solution. The solubility of compound I in 0.1M
NH.sub.4 OH and NaOH is about 23 mg/ml.
Chemical Synthesis II: 1.5 g polyaniline (dry emeraldine base form) was
dissolved into 40 ml concentrated sulfuric acid H.sub.2 SO.sub.4, and the
temperature slowly raised from the room temperature to 70.degree. C. in
water bath in 3 hour period with the constant stirring. The temperature
was kept at 70.degree. C. for 15 hours. Then the temperature was raised to
95.degree. C. within 0.5 hour and kept there for 4 hours. The reaction
mixture was cooled down to room temperature. The product was very slowly
added to -38.degree. C. ice made from 160 ml distilled H.sub.2 O in order
to precipitate the polymer. The temperature of the solution was not
allowed to reach higher than 0.degree. C. during the process. After the
temperature of the solution reached room temperature the solution was
filtered to obtain a fine powder of sulfonated polyaniline. Large
particles were obtained by subsequently heating the room temperature
solution up to 70.degree. C. in a two hour period, then cooling to room
temperature, and conducting filtration to separate the sulfonated
polyaniline from the solution. The sulfonated polyaniline was washed with
an excess of H.sub.2 O until the filtrate was neutral (as tested by pH
paper). Dry sulfonated polyaniline was obtained by pumping under dynamic
vacuum at room temperature for 48 hours.
Chemical Synthesis III: From the Chemical Synthesis II described above a
copolymer (i.e., the polymer mixture of polyanilines and sulfonated
polyaniline) was obtained by partially sulfonating polyaniline. This was
done in exactly the same way described in the Chemical Synthesis II except
utilizing shorter sulfonation times and/or lower sulfonation temperature.
Chemical Synthesis IV: Another way to prepare the copolymer
polyaniline-sulfonated polyaniline was to react 2-aminobenzene-sulfonic
acid (2ASA) with oxidizing agent in the presence of aniline. 10 g (0.58
mol) 2ASA and 2 ml (0.02 mol) aniline were dissolved in 500 ml 1M HCl. A
prepared solution of 6.609 g (0.029 mol) (NH.sub.4).sub.2 S.sub.2 O.sub.8
in 200 ml 1M HCl was added dropwise to the monomer solution with vigorous
stirring during a period of 10 minutes. After 1.5 hours, the precipitate
was collected on a Buchner funnel. The precipitate was washed with 1M HCl
until the filtrate was colorless. Then the precipitate was washed by 500
ml H.sub.2 O. To ensure that the copolymer was in its neutral form, the
precipitate was then transferred into a beaker containing 500 ml of
H.sub.2 O and stirred at room temperature for 4 hours. The mixture was
filtered until the pH of the filtrate was 7 . The dry copolymer was
obtained by pumping under dynamic vacuum at room temperature for 48 hours.
Chemical Synthesis V: The dry emeraldine base form of polyaniline is
exposed to SO.sub.3 gas for a predetermined length of time and at a
predetermined temperature. Gas phase sulfonation of the polyaniline at
elevated temperatures decreases the reaction time, while use of reduced
temperatures increases the reaction time. At conditions of excess SO.sub.3
gas, the gas phase sulfonation can be completed in about 12 hours at room
temperature.
Referring now to FIG. 2, one example of the process of gas phase
sulfonation is shown: finely ground dry emeraldine base form of
polyaniline powder 10 was placed in a container 12 having an open top 14
and a fine porosity glass frit bottom 16. The container 12 was placed
inside, in a spaced apart relationship, a closed container 20, containing
fuming sulfuric acid 22 H.sub.2 SO.sub.4 (SO.sub.3). The SO.sub.3 gaseous
fumes penetrate through the frit bottom 16 and surround the emeraldine
base polymer 10 through the open top 14 of the container 12 so as to come
into contact and react with the emeraldine base powders. The reaction time
depends upon such factors, as for example, the surface area, amount of
powder, and design of reactor. For example, 0.2 g of emeraldine base
powder (finely ground) spread over 3 cm diameter frit and exposed to 40 ml
of 23% fuming sulfuric acid sulfonated to one SO.sub.3 H per two rings in
about 8 hours. The resulting powder was fully soluble in 0.1M NH.sub.4 OH.
Referring now to FIG. 3, another example of gas phase sulfonation is shown:
finely ground dry emeraldine base form of polyaniline powder 30 is placed
in a first container or flask 32 having at least one opening 34. The first
flask 32 is placed in a spaced apart relationship, within a second
container or flask 40 containing fuming sulfuric acid 42 H.sub.2 SO.sub.4
(SO.sub.3). The first flask 32 is rotated about its longitudinal axis such
that the emeraldine base powder is homogeneously exposed to the SO.sub.3
gas fumes which enter the first flask 32 through the opening 34. The
reaction time for the configuration of FIG. 3 is considerably less than
the reaction time achieved by the approaches shown in FIG. 2.
Referring now to FIG. 4, yet another example of gas phase sulfonation is
shown: a film of dry emeraldine base formed of polyaniline 50 is suspended
in a closed container 52 containing fuming sulfuric acid 54. Since the gas
phase sulfonation process tends to soften the emeraldine base film, a
weight 56 can be attached to the lower end of the emeraldine base film 50.
The weight 56 stretches the film 50, thus providing an oriented sulfonated
polyaniline film. The SO.sub.3 gas rising from the fuming sulfuric acid
penetrates the emeraldine base film. For example, a film of emeraldine
base polymer having a thickness of 20 microns, exposed at room temperature
to fumes from 40 ml of 23% fuming sulfuric acid, sulfonated to one
SO.sub.3 H per 2 rings in about 2 hours. The resulting film was fully
soluble in 0.1M NH.sub.4 OH.
Films comprising the polyaniline emeraldine base polymer, already oriented
and either free standing or adhered to a substrate, and fibers comprising
the emeraldine base polyaniline can be sulfonated according to the
SO.sub.3 gas phase sulfonation method of the present invention.
It is also within the contemplated scope of the present invention that any
of the desired forms of the emeraldine base formed of polyaniline can be
sulfonated by exposure to SO.sub.3 gas without the presence of sulfuric
acid, H.sub.2 SO.sub.4.
Conductivities of the compound I was measured on compressed pellets of the
powder by using four point probe techniques with a Keithley 220 constant
current source and Keithley 181 voltmeter.
The conductivity of unoriented sulfonated polyaniline composition made
using the gas phase sulfonation process is in the range of about 0.03
S/cm. to about 0.1 S/cm.
Elemental analyses and conductivity studies are consistent with the
sulfonation of emeraldine base with fuming sulfuric acid proceeding to
give a self-doped, sulfonated, protonated forms of the emeraldine
oxidative state of polyaniline, the compound I which has a conductivity of
.about.0.1 S/cm. This polymer can be regarded as being formed by the
hypothetically initial formation of the strong acid, shown as structure b
in FIG. 1, which then immediately protonates the imine nitrogen atoms to
give the conducting polymer in an entirely analogous manner to strong
acids such as HCl. Treatment of the structure b compound with an aqueous
(ammonium) base yields the sulfonated, non-protonated insulating ammonium
salt forms analogous to emeraldine base, viz, the structure c compound
shown in FIG. 1.
The conductivity of the compound I (.sigma..about.0.1 S/cm) is similar to
that of emeraldine hydrochloride measured under the same experimental
conditions (.sigma..about.1- 5 S/cm; laboratory air), but lower than that
.sigma..about.18 S/cm of high molecular weight emeraldine hydrochloride.
The self-doped sulfonated polyaniline with emeraldine oxidative state
differs dramatically from nonexternally doped polyaniline in conductivity.
Since sulfonic acid is a strong acid, approximately as strong as
hydrochloric acid, the compound I is capable of doping itself. The dark
green self-doped compound I had a room temperature conductivity of about
0.1 S/cm in contrast to the purple color and insulating behavior of
polyaniline emeraldine base form. However, the conductivity of compound I
is lower than that of emeraldine hydrochloride pressed pellets.
The present invention thus discloses that sulfonated polyaniline can be
synthesized chemically. Elemental analyses and conductivity data suggest
that, depending on the sulfonation times and temperatures, the number of
--SO.sub.3 H groups per phenyl ring varied from 0.2 to 1.0. The
conductivity is independent of pH in the range of pH values smaller than
or equal to 7.
The present invention provides an uncomplicated and less time consuming
method for producing sulfonated polyaniline composition such that the
sulfonated polyaniline compositions and their derivatives are extremely
useful in various electronic, electrochemical, chemical, and optical
applications. The sulfonated polyaniline compositions have a more rapid
electrochemical response than polyaniline. The ability of the sulfonated
polyaniline compositions to have a fast switching speed between a
conducting and a nonconducting state with good reversibility makes such
compositions attractive polymers to use for a variety of electrochemical
applications.
Further, the solubility and the electrical conductivity of the sulfonated
polyaniline compositions makes such compositions especially useful in
still other applications. In addition, the process of the present
invention can be used to sulfonate previously oriented films, fibers, and
coatings produce self-protonated sulfonated polyaniline materials having
high conductivity, high mechanical strength and anisotropy.
The sulfonated polyaniline compositions can be coated by a variety of
techniques onto substrates of choice. The sulfonated polyaniline polymers
can be applied to substrates according to the present invention by spray
coating, dip coating, spin casting, transfer roll coating, brush-on
coating, and the like. The sulfonated polyaniline polymers can also be
electrochemically deposited onto conductive substrates by known
electrochemical deposition techniques.
Sulfonated polyaniline can also be entrained within a matrix of, or
copolymerized with, other polymer materials to thereby produce a blend or
a composite. Thus, sulfonated polyaniline could be dispersed in, for
example, polyethylene, polyimide, cellulose nitrate, and the like, and
also can be coated onto fibrous materials. The sulfonated polyaniline
compositions can be used with other insulating polymers to form conductive
thermosetting resins, epoxies, and thermoplastics, and reacted with
bismaleimides for use in forming, for example, such devices as conductive
seals, joints and moldings. In addition, derivatization of the sulfonated
polyaniline compositions can enhance compatibility and processability of
the polymer with other polymers.
In addition, the sulfonated polyaniline compositions can be cast as thin
films from a solvent solution, and the solvent evaporated to produce free
standing films. The sulfonated polyaniline films can be stacked as a
composite with other sulfonated polyaniline films, with films of
sulfonated polyaniline copolymerized with another polymer, or with
non-polyaniline polymers and/or copolymers. Depending on the desired type
and degree of substitution of the sulfonated polyaniline with various
crosslinkable functional moieties, the films produced can be cured in
deeper sections, that is, thicker films or articles can also be produced
by known polymer preparation techniques.
The sulfonated polyaniline compositions and derivatives thereof have, or
can be designed to have, desired processability in terms of, for example,
viscosity, flexural strengths, sol | | |