WO2007086288A1 - Procédé de production d’un dispositif activateur polymère conducteur - Google Patents

Procédé de production d’un dispositif activateur polymère conducteur Download PDF

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Publication number
WO2007086288A1
WO2007086288A1 PCT/JP2007/050569 JP2007050569W WO2007086288A1 WO 2007086288 A1 WO2007086288 A1 WO 2007086288A1 JP 2007050569 W JP2007050569 W JP 2007050569W WO 2007086288 A1 WO2007086288 A1 WO 2007086288A1
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electrolytic
conductive polymer
electrolytic solution
electrode
producing
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PCT/JP2007/050569
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English (en)
Japanese (ja)
Inventor
Susumu Hara
Tetsuji Zama
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Eamex Corporation
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Publication of WO2007086288A1 publication Critical patent/WO2007086288A1/fr

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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G61/00Macromolecular compounds obtained by reactions forming a carbon-to-carbon link in the main chain of the macromolecule
    • C08G61/12Macromolecular compounds containing atoms other than carbon in the main chain of the macromolecule
    • C08G61/122Macromolecular compounds containing atoms other than carbon in the main chain of the macromolecule derived from five- or six-membered heterocyclic compounds, other than imides
    • C08G61/123Macromolecular compounds containing atoms other than carbon in the main chain of the macromolecule derived from five- or six-membered heterocyclic compounds, other than imides derived from five-membered heterocyclic compounds
    • C08G61/124Macromolecular compounds containing atoms other than carbon in the main chain of the macromolecule derived from five- or six-membered heterocyclic compounds, other than imides derived from five-membered heterocyclic compounds with a five-membered ring containing one nitrogen atom in the ring

Definitions

  • the present invention relates to a conductive polymer actuator element made of polypyrrole.
  • An actuator using a conductive polymer can reduce the weight of the entire device incorporated because of its light weight, and can be used not only as a small drive device such as a micromachine but also as a large drive device. In particular, it is expected to be used for applications such as artificial muscles, robot arms, prosthetic hand actuators, and pumps.
  • a conductive polymer typified by polypyrrole not only has conductivity but also can incorporate ions as a dopant, and can be repeatedly doped and dedoped by applying a voltage. Therefore, the conductive polymer can exhibit electrolytic expansion and contraction, which is a phenomenon that expands or contracts due to electrochemical redox. This electrolytic expansion and contraction of the conductive polymer can be used as a drive for the actuator element.
  • Non-Patent Document 1 Genji, 4 others, “Highly Stretchable and Powerful Polypyrrole Linear Actuators”, Chemistry Letters, Japan Issue, 2003, No. 32 IV, No. 7, ⁇ 576-577 0
  • the electrolytic polymerization method is the most suitable method for producing a high-performance conductive high-molecular actuator.
  • electrolytes such as triflate and sulfoimide essential for high performance actuators are expensive, raising the cost of the actuator.
  • the electrolytic solution is repeatedly used for electrolytic polymerization, side reactions are likely to occur. Therefore, since the new electrolyte provides a higher-quality, higher-performance conductive polymer actuator, it is actually difficult to repeatedly use the electrolyte. Therefore, a manufacturing method that provides a high-performance conductive polymer activator film even when the electrolyte is repeatedly used is extremely important. Disclosure of the invention
  • An object of the present invention is to provide a production method for obtaining a high-performance conductive polymer actuator element that is almost equivalent to an actuator film before repetition even when the electrolytic solution is repeatedly used.
  • the present invention provides a method for producing a conductive polymer activator element capable of repeatedly producing a polypyrrole film by electrolytic polymerization on an electrode by repeatedly using a production electrolyte containing pyrrole.
  • a method for producing a conductive polymer actuator element was employed in which an electrolytic solution with a lowered electrolytic potential was repeatedly used for electrolytic polymerization on an electrode to repeatedly produce a polypyrrole film.
  • the present invention relates to a method for producing a conductive polymer activator element capable of repeating a polypyrrole film by electrolytic polymerization on an electrode by repeatedly using an electrolyte for production containing pyrrole.
  • a method for producing a conductive polymer actuator element characterized in that a polypyrrole film can be continued by electrolytic polymerization on an electrode in an electrolytic solution having a lowered electrolytic potential.
  • the means for lowering the electrolytic potential of the electrolytic solution is not limited, but it can be obtained, for example, by adding an acid, particularly trifluoroacetic acid.
  • the invention's effect is not limited, but it can be obtained, for example, by adding an acid, particularly trifluoroacetic acid.
  • the present invention is a method in which a polypyrrole film can be repeated by electrolytic polymerization on an electrode using an electrolytic solution with a lowered electrolytic potential, so that the polypyrrole is repeatedly used with the electrolytic solution without lowering the electrolytic potential.
  • the side reaction is suppressed and durability is improved.
  • the electrolyte is used repeatedly, it has almost the same high performance as the actuator membrane before repeated use.
  • a highly conductive polymer actuator element can be obtained. Therefore, since a good quality film can be obtained, the effect of cost reduction is remarkable.
  • the electrolytic polymerization proceeds easily, and not only a high-quality film and a high-performance actuator film can be obtained, but also the electrolytic solution can be used repeatedly. As a result, the manufacturing cost of the actuator can be significantly reduced.
  • FIG. 1 A triflate film on the electrode side (substrate side) according to the above-described Example 3 using CF 3 CO 3 H 2 H added
  • FIG. 2 is a scanning electron micrograph (1000 ⁇ SEM image data) showing a triflate film (polypyrrole film) on the same electrolyte side.
  • a polypyrrole film is obtained by electrolytic polymerization on an electrode in an electrolytic solution for producing pyrrole, preferably an electrolytic solution for producing an aromatic ester solution.
  • the present invention includes a step of using, as an electrolytic solution, an electrolytic solution prepared first or having a lower electrolytic potential than the subsequent electrolytic solution, and electropolymerization is performed on the electrode in the electrolytic solution with the lowered electrolytic potential.
  • electropolymerization is performed on the electrode in the electrolytic solution with the lowered electrolytic potential.
  • the electrolytic potential is lowered by adding trifluoroacetic acid, for example, as an acid to the subsequent electrolytic solution. It is also possible to repeat the electrolytic polymerization using the solution as it is, or repeat the process twice for the first electrolyte without lowering the electrolysis potential, and then lower the electrolysis potential for the electrolyte used for the third time, and then the electrolysis potential. It also includes repeated electrolytic polymerization without lowering. It is also possible to use an electrolytic solution obtained by lowering the electrolytic potential of the electrolytic solution prepared first.
  • pyrrole Since pyrrole has a low acidity potential and is easily polymerized, it does not lower the electrolysis potential by first adding an acid, etc., and the electrolysis potential is increased by adding acid or the like to the electrolyte to be used subsequently. It is preferable to employ a method of lowering.
  • an electrolytic solution of bis (perfluoroalkylsulfonyl) methide such as tris (trifluoromethylsulfol) methide salt cannot be used once and repeatedly, but for example, trifluoroacetic acid is added to 60cm3 of electrolytic solution.
  • lg when lg is added, a good quality film can be obtained even if it is repeated 10 times or more, and the performance of the actuator is improved.
  • Examples of the salt used in the electropolymerization include trifluoromethanesulfonate (triflate) and bis (perfluoroalkylsulfonyl) imide such as bis (trifluoromethylsulfol) imide salt.
  • Bis (perfluoroalkylsulfo) methide salts such as salts or tris (trifluoromethylsulfo) methide salts can be used.
  • trifluoromethane sulfonate (triflate) is used, a high-generation conductive polymer activator membrane can be obtained.
  • Bis (perfluoroalkylsulfonyl) imide salts such as bis (trifluoromethylsulfoyl) imide salts, or bis (perfluoroalkylsulfonyl) methides such as tris (trifluoromethylsulfol) methide salts
  • a salt is used, a highly stretchable conductive high molecular weight activator film can be obtained.
  • Trifluoromethanesulfonate ion (triflate) is represented by the chemical formula CF 2 SO—.
  • the polypyrrole film obtained by the production method of the present invention has excellent tensile strength and good tensile elongation at break. It will be a strong sword.
  • the content of the trifluoromethanesulfonate ion in the electrolyte is not particularly limited, but it is preferably 0.1 to 30% by weight in the electrolyte. More preferably, it is contained by weight.
  • N (n is an integer), that is, used as an electrolyte containing bis (perfluoroalkylsulfo) imide ion.
  • this electrolyte contains bis (trifluoromethylsulfonyl) imide ion. Electrolyte is preferred.
  • perfluoroalkylsulfol group examples include a pentafluorosulfonylsulfonyl group, a heptafluoropropylsulfol group, a nonafluorobutylsulfol group, Decafluoropentyl sulfol group, tridecafluoro hexyl sulphonyl group, pentadecafluoro sulphate butyl sulphonyl group, heptadecafluoro octyl sul A phonyl group etc. can be mentioned.
  • the content of these electrolytes is not particularly limited, but is preferably 0.1 to 30% by weight, more preferably 1 to 15% by weight in the electrolytic solution.
  • Examples of the perfluoroalkylsulfonyl group include trifluoromethylsulfonyl group, pentafluoroethylsulfonyl group, heptafluoropropylsulfol group, and nonafluorobutyl. Examples include sulfole group, undecafluoropentyl sulfol group, tridecafluoro hexyl sulpho group, pentadeca fluor butyl butyl group, hepta decafluorooctyl sulphonyl group, etc. .
  • the perfluoroalkylsulfurmethide ion that can be contained in the electrolytic solution of the electropolymerization method can form a salt with a cation, and the perfluoroalkylsulfonulmetide salt is used as an electropolymerization method.
  • the electrolyte solution in The cation that forms a salt with the perfluoroalkylsulfurmethide may be composed of one or more elements, such as Li +.
  • the cation is not particularly limited as long as it is a Lewis acid that can form a perfluoroalkylsulfurmethide ion as a monovalent cation and can be cleaved in an electrolytic solution.
  • the cation is a metal element, for example, an element selected from alkali metals such as lithium can be used. Further, when the cation is a molecule, for example, an alkylammonium represented by tetraptyl ammonium, tetraethylammonium, pyridinium, imidazolium, or the like can be used.
  • perfluorosulfo-lmethide salt is easily dissociated in solution and easily available, tris (trifluoromethylsulfo) methidolithium, tris (pentafluoroeluene) Tris (perfluoroalkylsulfol) methidelithium such as tilsulfol) methidelithium, and tris (trifluoromethylsulfol) methide and tris Tetraptyl ammonium salts, pyridinium salts or imidazolium salts for tris (perfluoroalkylsulfol) methides such as ntafluoroethyl sulfo) methide are preferred.
  • the electrolytic solution (electrolytic solution for producing a conductive polymer) used for the electrolytic polymerization is at least one of an ether bond, an ester bond, a carbonate bond, a hydroxyl group, a nitro group, a sulfone group, and a -tolyl group. It is preferable to use an organic compound containing a bond or a functional group, and Z, or a Rogeny hydrocarbon as a solvent.
  • Examples of the organic compound include 1,2 dimethoxyethane, 1,2 diethoxyethane, tetrahydrofuran, 2-methyltetrahydrofuran, 1,4 dioxane (an organic compound containing an ether bond), ⁇ -butyrolataton, ethyl acetate, ⁇ -butyl acetate, tert-butyl acetate, 1,2-diacetoxetane, 3-methyl-2-oxazolidinone, methyl benzoate, ethyl benzoate, butyl benzoate, dimethyl phthalate, jetyl phthalate (or more ester bond)
  • Organic compounds containing) propylene carbonate, ethylene carbonate, dimethyl carbonate, jetyl carbonate, methyl ethyl carbonate (above, organic compounds containing a force-bonate bond), ethylene glycol, butanol, 1-hexanol, cyclohexanol , 1-octano
  • the organic compound containing a hydroxyl group is not particularly limited, but is preferably a polyhydric alcohol or a monohydric alcohol having 4 or more carbon atoms because of its good force expansion / contraction rate.
  • the organic compound has two or more bonds or functional groups among ether bonds, ester bonds, carbonate bonds, hydroxyl groups, nitro groups, sulfone groups and -tolyl groups in the molecule.
  • Organic compounds may be included in any combination.
  • the halogenated hydrocarbon contained as a solvent in the electrolytic solution for producing the conductive polymer Is not particularly limited as long as at least one or more hydrogen atoms in the hydrocarbon are substituted with halogen atoms and can stably exist as a liquid under electrolytic polymerization conditions.
  • the halogenated hydrocarbon include dichloromethane and dichloroethane. Only one kind of the halogenated hydrocarbon can be used as a solvent in the electrolytic solution for producing a conductive polymer, but two or more kinds can be used in combination.
  • the halogenated hydrocarbon may be used in the form of a mixture with the above organic compound as a solvent in the electrolytic solution for producing the conductive polymer.
  • the content of the perfluoroalkylsulfurmethide ion in the electrolytic solution in the electrolytic polymerization method is not particularly limited, but in order to ensure sufficient ionic conductivity of the electrolytic solution,
  • the perfluoroalkylsulfomethide salt is preferably contained in the electrolyte in an amount of 1 to 40% by weight, more preferably 2.8 to 20% by weight.
  • a composite electrolyte in which 1 to 80% of trifluoromethansulfonate is added to the electrolyte can be used.
  • the electrolytic solution (electrolytic solution for producing a conductive polymer) used in the electrolytic polymerization method further contains a monomer of a conductive polymer, and further, a known polymer such as polyethylene glycol or polyacrylamide is used. Other additives can also be included.
  • the electropolymerization method a known electropolymerization method can be used as the electropolymerization of the conductive polymer monomer, and any of a constant potential method, a constant current method, and an electric sweep method can be used. Can be used.
  • the electropolymerization method can be performed at a current density of 0.01 to 20 mAZcm 2 and a reaction temperature of 70 to 80 ° C. In order to obtain a conductive polymer having a good film quality, the current density is set to 0. It is more preferable that the reaction temperature is 30 to 30 ° C, which is preferably performed under conditions of l to 2mAZcm 2 and reaction temperature of 40 to 40 ° C! /.
  • the working electrode used in the electropolymerization method is not particularly limited as long as it can be used for electropolymerization, and a carbon electrode, a metal electrode, an ITO glass electrode, and the like can be used. It is preferable to use a single carbon electrode.
  • a metal electrode it is not particularly limited as long as it is a metal-based electrode, but it is selected from the group consisting of Pt, Ti, Ni, Au, Ta, Mo, Cr and W. Metal element In addition, any single metal electrode or alloy electrode can be preferably used.
  • a known electrode such as Pt or Ni can be preferably used.
  • the force S that uses pyrrole and further polymerized by acid polymerization by electrolytic polymerization to increase the conductivity.
  • the monomer compounds shown can be combined. Examples thereof include hetero five-membered cyclic compounds such as thiophene and isothianaphthene, and derivatives such as alkyl groups and oxyalkyl groups thereof. Of these, complex five-membered cyclic compounds such as thiophene and derivatives thereof are preferred.
  • the conductive polymer polymerized on the working electrode is obtained by washing in acetone using a solvent that can swell the conductive polymer such as acetone after electrolytic polymerization.
  • a conductive polymer film can be easily obtained.
  • a glassy carbon electrode is used as the working electrode, fine pores are generated on the working electrode side, and the polypyrrole film can be easily peeled off due to the working electrode force, compared with the polyimide of sulfoimide described above.
  • a polypyrrole film of the methide having a large area can be obtained, and a tubular polypyrrole can be easily produced.
  • the polypyrrole triflate film can be used in a thickness of, for example, 50 ⁇ m or less, and the sulfoimide film or the methide film can be used in a thickness of, for example, 200 m or less.
  • the actuator element is driven by applying a voltage to the polypyrrole film in a driving electrolyte containing a driving electrolyte.
  • the driving electrolyte used for driving the actuator element includes an electrolyte for driving the actuator element by voltage application, and includes a solvent for dissolving the electrolyte.
  • a solvent for dissolving the electrolyte By including a mixed solvent of water and an organic solvent as a solvent for dissolving the electrolyte, an actuator element containing a conductive polymer measures the amount of expansion and contraction (driving speed) with respect to time in a state where a constant voltage is applied. In this case, a large driving speed can be shown in the driving electrolyte.
  • the drive electrolyte contained in the drive electrolyte is, for example, NaPF, trifluoromethanesulfonate ions, or the like, as used in the electrolyte solution for production. It is desirable to include an ion of bisimide or the imide salt thereof, or an ion of bis (trifluoromethylsulfol) methide or tris (trifluoromethylsulfo) methide or the methide salt thereof. Lithium, sodium, etc. are used as the other ion constituting the salt
  • LiTFSI PCZH 2 O propylene carbonate water
  • the organic solvent contained in the driving electrolyte solution is not particularly limited, but is preferably a polar organic solvent that can be used as an electrochemical reaction field.
  • the organic solvent is preferably an organic solvent selected from the group consisting of propylene carbonate, y-butylate ratatone, ethylene carbonate, dimethyl carbonate, jetyl carbonate, and acetonitrile, particularly propylene carbonate, ethylene carbonate.
  • the preferred propylene carbonate is more preferable because the organic solvent in which the group strengths of bonate, y-petit-mouth rataton and acetonitrile are also selected can obtain a high stretch rate and a large maximum stretch rate.
  • the mixing ratio of water and the organic solvent in the mixed solvent is not particularly limited.
  • the driving speed can be improved more than twice as compared with the case where only the organic solvent is used.
  • the minimum value of the polar organic solvent for improving the driving speed due to the ability of the organic solvent to swell the conductive polymer depends on the type of the polar organic solvent.
  • the water content of the special grade reagent is 0.005%, so the mixing ratio of water and polar organic solvent can be 0.1: 99.9.
  • a preferable range of the mixing ratio of water and the polar organic solvent in the mixed solvent is a volume ratio, and a water content is determined from a value selected from a lower limit of the water content ratio of 0.5, 1.0, 5.0, 10, or 20.
  • It lower limit upper limit force 99.5, 99.0, 95.0, 90.0, or ⁇ 80.0 force can be selected according to the type of the polar organic solvent.
  • the mixing ratio is determined by analyzing the driving electrolyte by using a measuring method using a gas chromatographic method, particularly a measuring method using a Karl Fascher method if the water content is low. By seeking Togashi.
  • the mixing specific force capacity ratio of water and propylene carbonate is 25:75 to 75:25. This is preferable because the driving speed by applying a voltage to the conductive polymer becomes faster.
  • the mixed solvent may use a plurality of polar organic solvents. In this case, the mixing ratio is calculated by the ratio of the weight of water to the total weight of all polar organic solvents.
  • the water is not particularly limited, but is preferably distilled water or ion-exchanged water. 1S is preferable because an inhibitor of electrolytic stretching due to metal ions, salt ions, and the like is hardly included. .
  • the temperature of the driving electrolyte in the actuator element driving method of the present invention is not particularly limited. However, in order to cause the conductive polymer to be subjected to electrolytic expansion and contraction at a higher speed, a speed of 10 to 100 is required. It is preferable that the temperature is ° C, more preferably 40 to 80 ° C. Further, the concentration of the cation in the driving electrolyte solution is not particularly limited, but is 0.1 to 5. Omol / L because a large expansion / contraction ratio can be obtained and the driving can be stably performed. Good for! /
  • the actuator element including the polypyrrole is placed in the driving electrolyte, and a counter electrode is installed in the driving electrolyte, so that the conductive polymer and the counter electrode are disposed.
  • the actuator element is driven.
  • the voltage is not particularly limited.
  • a voltage having an absolute value of applied voltage (V) of 0.2 to 5.0 can be applied for the expansion and contraction of the actuator element.
  • the absolute value of the applied voltage (V) is 0.5 to 5.0 for the expansion and contraction movement of the actuator element.
  • the applied voltage may have an upper limit appropriately depending on the use of the conductive polymer composition element.
  • DMPIMe 2-dimethyl-3-Puropirui Midazoriumu tris
  • DMPIMe 2-dimethyl-3-Puropirui Midazoriumu tris (triflate Ruo b methylsulfonyl) methide
  • the maximum stretching ratio measured by electrolytic stretching at a sweep rate of 2 mVZs in the potential range of 0.9 V to +0.7 V vs. AgZAg + in a mixed solution of Z water (lZl) was 30.0%. Furthermore, when the polypyrrole film was contracted at a constant potential of ⁇ 0.7V vs. AgZAg + in the same driving electrolyte, the contraction rate was 3.0% in 2 seconds, 7.3% in 5 seconds, and 10 seconds. It was 12.9% at 100 seconds and 28.0% at 100 seconds.
  • the electrolytic solution used in this electrolytic polymerization was again used to carry out the same electrolytic polymerization as described above, and a similar polypyrrole film could be obtained.
  • a homogeneous film was not obtained, and polypyrrole was deposited in a streaky pattern on the glassy carbon electrode (GC electrode). This precipitate was so powerful that it could not be driven as an actuator.
  • the maximum expansion / contraction rate is a value obtained by dividing the maximum length displaced due to expansion / contraction by the original length of the polypyrrole film, and the contraction rate is the length displaced by contraction as the original length of the polypyrrole film. The value divided by. The same applies hereinafter.
  • a polypyrrole film was obtained on the electrode by electropotential polymerization at + 1.4V vs. AgZAgCL for 8 hours.
  • the performance of the actuator is shown in Table 1 and Table 2.
  • a polypyrrole actuator exhibiting high speed and large elongation was obtained.
  • the acid addition amount was as large as 4.777 g, the conductivity of the film was lowered and the performance of the actuator was also low. It is thought that the electrolyte was degraded by acid.
  • FIG. 1 A scanning electron microscope (SEM) photograph of polypyrrole prepared by acid addition was shown in Fig. 1. The film was extremely homogeneous, smooth and dense.
  • the manufacturing method of the present invention can be used for the manufacturing method of an actuator element in all fields to which the driving of the actuator element can be applied using electrolytic expansion and contraction of a conductive polymer.
  • it can be suitably used as a production method for applications such as artificial muscles, robot arms, prosthetic hand actuators, and pumps.

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  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Polyoxymethylene Polymers And Polymers With Carbon-To-Carbon Bonds (AREA)
  • Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)

Abstract

La présente invention concerne un procédé de production d’un dispositif activateur polymère conducteur qui maintient essentiellement les mêmes performances élevées, malgré une utilisation répétée d'une solution électrolytique, que celles de la membrane de l'activateur avant la répétition. Elle concerne un procédé de production d’un dispositif activateur polymère conducteur, consistant à réaliser une polymérisation électrolytique sur une électrode par l'utilisation répétée d'une solution électrolytique productive contenant du pyrrole pour obtenir ainsi de façon répétée une pellicule de polypyrrole, un acide étant ajouté à la solution électrolytique après avoir obtenu la pellicule de polypyrrole par polymérisation électrolytique sur l’électrode pour diminuer ainsi le potentiel électrolytique, et la polymérisation électrolytique étant réalisée sur l’électrode dans la solution électrolytique avec le potentiel électrolytique diminué de façon à obtenir la pellicule de polypyrrole avec succès.
PCT/JP2007/050569 2006-01-24 2007-01-17 Procédé de production d’un dispositif activateur polymère conducteur WO2007086288A1 (fr)

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US10892523B2 (en) * 2016-10-27 2021-01-12 Toyota Motor Engineering & Manufacturing North America, Inc. Aqueous electrolyte with carbonate and batteries using the same
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Publication number Priority date Publication date Assignee Title
WO2005026230A1 (fr) * 2003-09-10 2005-03-24 Eamex Corporation Procede permettant de produire un polymere electroconducteur
WO2005100438A1 (fr) * 2004-04-15 2005-10-27 Eamex Corporation Procédé de fabrication de film polypyrrole
JP2006054951A (ja) * 2004-08-10 2006-02-23 Eamex Co 導電性高分子アクチュエータ素子の駆動方法
JP2006274229A (ja) * 2005-03-26 2006-10-12 Eamex Co 導電性高分子アクチュエータ素子の駆動方法
WO2007010747A1 (fr) * 2005-07-19 2007-01-25 Eamex Corporation Élément activateur polymérique conducteur

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JPH03166225A (ja) * 1989-11-25 1991-07-18 Toyobo Co Ltd 導電性重合体およびその製造方法
JP3346346B2 (ja) * 1999-02-10 2002-11-18 松下電器産業株式会社 固体電解質形成用重合液とその製造方法

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2005026230A1 (fr) * 2003-09-10 2005-03-24 Eamex Corporation Procede permettant de produire un polymere electroconducteur
WO2005100438A1 (fr) * 2004-04-15 2005-10-27 Eamex Corporation Procédé de fabrication de film polypyrrole
JP2006054951A (ja) * 2004-08-10 2006-02-23 Eamex Co 導電性高分子アクチュエータ素子の駆動方法
JP2006274229A (ja) * 2005-03-26 2006-10-12 Eamex Co 導電性高分子アクチュエータ素子の駆動方法
WO2007010747A1 (fr) * 2005-07-19 2007-01-25 Eamex Corporation Élément activateur polymérique conducteur

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