WO2012147872A1 - 新規なポリビニルスルホン酸、その製造方法及びその用途 - Google Patents
新規なポリビニルスルホン酸、その製造方法及びその用途 Download PDFInfo
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- WO2012147872A1 WO2012147872A1 PCT/JP2012/061264 JP2012061264W WO2012147872A1 WO 2012147872 A1 WO2012147872 A1 WO 2012147872A1 JP 2012061264 W JP2012061264 W JP 2012061264W WO 2012147872 A1 WO2012147872 A1 WO 2012147872A1
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F28/00—Homopolymers and copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a bond to sulfur or by a heterocyclic ring containing sulfur
- C08F28/02—Homopolymers and copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a bond to sulfur or by a heterocyclic ring containing sulfur by a bond to sulfur
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- C08L41/00—Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a bond to sulfur or by a heterocyclic ring containing sulfur; Compositions of derivatives of such polymers
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- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L65/00—Compositions of macromolecular compounds obtained by reactions forming a carbon-to-carbon link in the main chain; Compositions of derivatives of such polymers
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- C09D141/00—Coating compositions based on homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a bond to sulfur or by a heterocyclic ring containing sulfur; Coating compositions based on derivatives of such polymers
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01B—CABLES; CONDUCTORS; INSULATORS; SELECTION OF MATERIALS FOR THEIR CONDUCTIVE, INSULATING OR DIELECTRIC PROPERTIES
- H01B1/00—Conductors or conductive bodies characterised by the conductive materials; Selection of materials as conductors
- H01B1/06—Conductors or conductive bodies characterised by the conductive materials; Selection of materials as conductors mainly consisting of other non-metallic substances
- H01B1/12—Conductors or conductive bodies characterised by the conductive materials; Selection of materials as conductors mainly consisting of other non-metallic substances organic substances
- H01B1/124—Intrinsically conductive polymers
- H01B1/127—Intrinsically conductive polymers comprising five-membered aromatic rings in the main chain, e.g. polypyrroles, polythiophenes
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01G—CAPACITORS; CAPACITORS, RECTIFIERS, DETECTORS, SWITCHING DEVICES OR LIGHT-SENSITIVE DEVICES, OF THE ELECTROLYTIC TYPE
- H01G9/00—Electrolytic capacitors, rectifiers, detectors, switching devices, light-sensitive or temperature-sensitive devices; Processes of their manufacture
- H01G9/0029—Processes of manufacture
- H01G9/0036—Formation of the solid electrolyte layer
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01G—CAPACITORS; CAPACITORS, RECTIFIERS, DETECTORS, SWITCHING DEVICES OR LIGHT-SENSITIVE DEVICES, OF THE ELECTROLYTIC TYPE
- H01G9/00—Electrolytic capacitors, rectifiers, detectors, switching devices, light-sensitive or temperature-sensitive devices; Processes of their manufacture
- H01G9/004—Details
- H01G9/022—Electrolytes; Absorbents
- H01G9/025—Solid electrolytes
- H01G9/028—Organic semiconducting electrolytes, e.g. TCNQ
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01G—CAPACITORS; CAPACITORS, RECTIFIERS, DETECTORS, SWITCHING DEVICES OR LIGHT-SENSITIVE DEVICES, OF THE ELECTROLYTIC TYPE
- H01G9/00—Electrolytic capacitors, rectifiers, detectors, switching devices, light-sensitive or temperature-sensitive devices; Processes of their manufacture
- H01G9/004—Details
- H01G9/04—Electrodes or formation of dielectric layers thereon
- H01G9/042—Electrodes or formation of dielectric layers thereon characterised by the material
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G2261/00—Macromolecular compounds obtained by reactions forming a carbon-to-carbon link in the main chain of the macromolecule
- C08G2261/10—Definition of the polymer structure
- C08G2261/14—Side-groups
- C08G2261/142—Side-chains containing oxygen
- C08G2261/1424—Side-chains containing oxygen containing ether groups, including alkoxy
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G2261/00—Macromolecular compounds obtained by reactions forming a carbon-to-carbon link in the main chain of the macromolecule
- C08G2261/30—Monomer units or repeat units incorporating structural elements in the main chain
- C08G2261/32—Monomer units or repeat units incorporating structural elements in the main chain incorporating heteroaromatic structural elements in the main chain
- C08G2261/322—Monomer units or repeat units incorporating structural elements in the main chain incorporating heteroaromatic structural elements in the main chain non-condensed
- C08G2261/3223—Monomer units or repeat units incorporating structural elements in the main chain incorporating heteroaromatic structural elements in the main chain non-condensed containing one or more sulfur atoms as the only heteroatom, e.g. thiophene
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G2261/00—Macromolecular compounds obtained by reactions forming a carbon-to-carbon link in the main chain of the macromolecule
- C08G2261/70—Post-treatment
- C08G2261/79—Post-treatment doping
- C08G2261/794—Post-treatment doping with polymeric dopants
Definitions
- the present invention relates to polyvinyl sulfonic acid, its production method and its use.
- sulfonic acids are mainly used, and low molecular sulfonic acids and / or high molecular weight sulfonic acids are used (for example, see Patent Documents 1 and 2).
- High molecular weight sulfonic acids are known to have an advantage of maintaining a stable interaction with a conductive polymer as compared to low molecular weight sulfonic acids (see, for example, Patent Document 3).
- PESs polystyrene sulfonic acids
- PVS polyvinyl sulfonic acids
- Japanese Patent No. 3040113 Japanese Patent No. 2636968 Japanese Patent No. 3066431 Japanese Patent No. 4077675 JP 2010-195980 A
- the PSSs described in Patent Documents 2 and 4 contain an aromatic ring in addition to a sulfonic acid group serving as a dopant and a polyethylene main chain forming a polymer structure, and components other than a conductive polymer of an electron transfer body When the ratio is increased, the conductivity per weight is reduced when the conductive film is formed.
- the PVS described in Patent Document 5 precipitates immediately after the formation of the conductive polymer-dopant complex obtained by polymerization of the conductive polymer in the polymer aqueous solution and / or suspension. There is a problem that a stable dispersion cannot be obtained.
- the ratio of the polyethylene main chain to the sulfonic acid is high, and no organic solvent is required to improve conductivity, and stable dispersion of the conductive polymer-dopant complex is achieved.
- the present invention provides a polymer sulfonic acid dopant capable of producing a dispersion of a stable conductive polymer-dopant complex, a polyvinyl sulfonic acid having a high ratio of polyethylene main chain to sulfonic acid, and a method for producing the same.
- the dispersion and its manufacturing method in particular, a dispersion that can be made highly conductive only with an aqueous solvent, a conductive film having high electrical conductivity using the dispersion, and an organic material including the conductive film are provided. This is the main issue.
- the present inventors have found that the above-mentioned problems can be solved by using polyvinyl sulfonic acid having a special configuration as a polymer dopant, and have completed the present invention.
- the conductive polymer is polymerized in the presence of the dopant aqueous solution or suspension, and the resulting dispersion is stable and has high conductivity even when no organic solvent is added (for example, more than 10 S / cm).
- the inventors have found that a conductive film is to be formed and have completed the present invention.
- the present invention relates to the following polyvinyl sulfonic acid and a production method thereof, a conductive polymer dispersion and a production method thereof, a conductive film using the dispersion, and the like.
- the molar amount of the sulfonic acid group derived from the vinyl sulfonic acid monomer is 50.0 to 98.0 mol% with respect to the molar amount of all the monomer units, and the absorbance is 0.1 or more in the wavelength range of 255 to 800 nm (aqueous solution 0.
- the method for producing polyvinyl sulfonic acid according to any one of [1] to [4], comprising a step of heating the polyvinyl sulfonic acid at a temperature exceeding 60 ° C.
- [8] [1] A composite comprising the polyvinyl sulfonic acid according to any one of [4] and a conductive polymer.
- the polyvinyl sulfonic acid according to any one of [1] to [4] is dissolved and / or dispersed in a solvent, and the monomers of the conductive polymer are polymerized in the dissolved and / or dispersed solvent.
- a dispersion for forming a conductive film contains poly (3,4-ethylenedioxythiophene); In the reflection method XDR measurement of the conductive film, the peak area ratio (peak K area / peak L area) between the peak K in the range 2 ⁇ of 8 ° to 10 ° and the peak L in the range 2 ⁇ of 24 ° to 28 °.
- the dispersion liquid according to [16] comprising a conductive polymer and a polyanion.
- the conductive composite using the polyvinyl sulfonic acid of the present invention as a dopant for a conductive polymer has very high stability in a dispersion and exhibits high conductive performance without adding a high-boiling organic solvent.
- a conductive film can be manufactured. Due to the high stability of the dispersion, the decrease in the conductive performance due to the addition of the film physical property improving agent is small, and the film physical properties for various conductive applications can be improved.
- FIG. 1 is an example of measurement results of solid-state NMR of polyvinyl sulfonic acid obtained in this example.
- FIG. 2 is an example of the solid-state NMR measurement results of the conductive film obtained in this example.
- the present embodiment a mode for carrying out the present invention (hereinafter referred to as “the present embodiment”) will be described in detail.
- this invention is not limited to the following embodiment, It can implement by changing variously within the range of the summary.
- the polyvinyl sulfonic acid of the present embodiment is a polyvinyl sulfonic acid containing a vinyl sulfonic acid unit represented by the following general formula (1), [Wherein R 1 , R 2 and R 3 are each independently hydrogen, an alkyl group having 1 to 15 carbon atoms or an alkylene group, and Z is hydrogen, halogen, an alkyl group having 1 to 15 carbon atoms or An alkylene group, a metal ion, an ammonium ion, a protonated primary, secondary or tertiary amine, or a quaternary ammonium ion]
- the molar amount of the sulfonic acid group derived from the vinyl sulfonic acid monomer is 50.0 to 98.0 mol% with respect to the molar amount of all the monomer units, and the absorbance is 0.1 or more in the wavelength range of 255 to 800 nm (aqueous solution 0. 2 mass%,
- R 1 , R 2 and R 3 in the above formula specific examples of the alkyl group having 1 to 15 carbon atoms are not particularly limited, but include a methyl group, an ethyl group, an n-propyl group, an isopropyl group, an n-butyl group. Group, isobutyl group, sec-butyl group, tert-butyl group, n-pentyl group, isopentyl group, neopentyl group, tert-pentyl group and the like.
- R 1 , R 2 and R 3 in the above formula specific examples of the alkylene group having 1 to 15 carbon atoms are not particularly limited, but ethylene group, n-propylene group, n-butylene group, n- Examples include a hexylene group, an n-heptylene group, an n-octylene group, and an n-dodecylene group.
- the polyvinyl sulfonic acid of this Embodiment is useful as a polymer dopant for conductive polymers.
- the conductive polymer in which the polyvinyl sulfonic acid of this embodiment acts as a dopant refers to a polymer having a structure in which double bonds and single bonds are alternately long in the polymer structure.
- the conductive polymer is not particularly limited.
- the conductive polymer may be a specific polymer of this embodiment. From the viewpoint of polymerizability in water in which nylsulfonic acid is dissolved or dispersed, heteroaromatics are preferable, polypyrrole and polythiophene are more preferable.
- the alkyl group may be linear or branched, and specific examples include a methyl group, an ethyl group, and a propyl group.
- alkylene group examples include a methylene group, an ethylene group, and a propylene group.
- the substituent that the alkylene group may have is not particularly limited, and examples thereof include a methyl group, an ethyl group, a hydroxymethyl group, and a hydroxyethyl group.
- the vinyl sulfonic acid monomer forming the polyvinyl sulfonic acid of the present embodiment is represented by the following general formula (1) ′.
- R 1 , R 2 and R 3 are each independently hydrogen, an alkyl group having 1 to 15 carbon atoms or an alkylene group, and Z is hydrogen, halogen, an alkyl group having 1 to 15 carbon atoms or An alkylene group, a metal ion, an ammonium ion, a protonated primary, secondary or tertiary amine, or a quaternary ammonium ion]
- a compound in which sulfonic acid is directly bonded to a vinyl group.
- Such vinyl sulfonic acid monomers are not particularly limited, and examples thereof include alkyl-substituted vinyl sulfonic acids such as 1-alkyl vinyl sulfonic acid, 2-alkyl vinyl sulfonic acid, and 1,2-alkyl sulfonic acid; sodium vinyl sulfonate Sulfonates such as sodium 1-alkylvinylsulfonate, potassium vinylsulfonate, ammonium vinylsulfonate, alkylamine salt of vinylsulfonate; sulfonate halides such as vinylsulfonate fluoride, vinylsulfonate chloride; vinyl sulfonate And the like as typical vinyl sulfonic acid monomers.
- vinyl sulfonates and vinyl sulfonates in which R 1 , R 2 , and R 3 are hydrogen and Z is hydrogen, sodium, or potassium are preferable monomers.
- this vinyl sulfonic acid monomer does not have a phenyl group or the like between the polymer main chain and the sulfonic acid group, the sulfonic acid group weight with respect to the polymer weight becomes very high, and the doping amount with respect to the polymer dopant weight is very high. And an excellent dopant can be formed.
- Molar amount of all monomer units in the polymer means that the polymer constituting monomer is a monomer having multiple bonds, and the polymer is polymerized. This is the molar amount of the polymer constituting monomer when the polymer is constituted by the monomer having the maximum molar amount of the monomer for the purpose.
- Polyvinyl sulfonic acid in which the molar amount of the sulfonic acid group derived from the vinyl sulfonic acid monomer is within a specific range with respect to the molar amount of all the monomer units.
- the polyvinyl sulfonic acid of the present embodiment it is derived from the vinyl sulfonic acid monomer in the polymer.
- the sulfonic acid group is preferably used as a conductive polymer doping agent. This sulfonic acid group does not have a phenyl group or the like between the polymer main chain and the sulfonic acid group.
- the polyvinyl sulfonic acid of the present embodiment is an excellent doping agent having a very high sulfonic acid group weight relative to the polymer weight and a very high doping amount relative to the polymer dopant weight.
- the sulfonic acid group easily moves due to the movement of the polymer main chain and has a problem that the state of doping into the conductive polymer becomes unstable, but in this embodiment, The amount of the sulfonic acid group in which the movement of the sulfonic acid group is less affected by the movement of the polymer main chain can be found, and a conductive polymer-dopant complex that is higher and more stable than the polyvinyl sulfonic acid can be produced.
- the molar amount of the sulfonic acid group derived from the vinyl sulfonic acid monomer is set in the range of 50.0 to 98.0 mol% with respect to the molar amount of all monomer units in the polymer.
- the molar amount (mol%) of the sulfonic acid group derived from the vinyl sulfonic acid monomer is equal to or higher than the lower limit, the doping amount per polymer weight is improved.
- the amount is not more than the upper limit, the sulfonic acid group is hardly affected by the movement of the polymer main chain, and a stable conductive polymer-dopant complex can be formed.
- the preferred molar amount of the sulfonic acid group is 85.0 to 97.0 mol%.
- the molar amount of the sulfonic acid group can be achieved by heat-treating polyvinylsulfonic acid described later, or by blending a crosslinking agent.
- the sulfonic acid group includes an anhydride obtained by dehydration condensation of two molecules of sulfonic acid.
- Polyvinylsulfonic acid containing an anhydride that has been heat-treated and dehydrated and condensed with two molecules of sulfonic acid groups simultaneously with desulfonation is a preferred polymer.
- a desulfonic acid treatment such as heating to adjust the molar amount of the sulfonic acid group derived from the vinyl sulfonic acid monomer, derived from the vinyl sulfonic acid monomer in the polyvinyl sulfonic acid
- a method for measuring the molar amount of the sulfonic acid group a method of measuring the molar amount of the sulfonic acid group by titrating the taken-out solid with a base such as NaOH after the desulfonic acid treatment is adopted.
- the obtained solution was subjected to 0.1 mol made by Sigma Aldrich using a potentiometric automatic titrator AT-610 made by Kyoto Electronics Industry Co., Ltd. This can be determined by performing potentiometric titration using / L sodium hydroxide or the like as a titrant and applying to the following formula (1).
- the unit of the molar concentration of the titrant is mol / L
- V is the titration amount (mL) of the titrant
- 108 is the molecular weight (g / mol) of vinyl sulfonic acid.
- W is the mass (g) of the extracted solid
- f is the calibration factor of the titrant.
- the ratio (mol%) of the molar amount of the sulfonic acid group derived from the vinyl sulfonic acid monomer to the molar amount of all the monomer units is 50.0 to 98.0 mol%.
- the molecular weight of the polyvinyl sulfonic acid of the present embodiment is not particularly limited, but there is a preferable range depending on how it is used as a conductive product. That is, when the conductive polymer-dopant complex is molded into a film and used, the weight average molecular weight of the polyvinyl sulfonic acid of the present embodiment is in the range of 2,000 to 1,000,000. In order to develop higher conductive performance, it is preferably in the range of 10,000 to 800,000.
- Examples of a method for obtaining polyvinyl sulfonic acid having a weight average molecular weight within the above range include a method of adjusting the monomer concentration, polymerization temperature and polymerization initiator concentration in a timely manner in polymerization methods such as radical polymerization, cationic polymerization and anionic polymerization. It is done.
- the weight average molecular weight can be obtained by gel permeation chromatograph (GPC) measurement.
- GPC gel permeation chromatograph
- aqueous solutions of standard polyethylene oxides having molecular weights of 900000, 250,000, 107000, 50000, 21000, and 4100 manufactured by Tosoh Corporation are prepared and used, and a high-speed GPC device HLC-8320 manufactured by Tosoh Corporation is used. Can be measured.
- TSK-GEL ⁇ guard column manufactured by Tosoh Corporation, ⁇ -2500, ⁇ -3000, ⁇ -4000, and the like can be used, and these may be connected.
- the measurement conditions of the apparatus can be set as appropriate, but a column temperature of 40 ° C., a flow rate of 1.0 ml / min, etc. are preferable measurement conditions.
- GPC measurement of each polymer can be performed by injecting an analysis sample into a GPC apparatus and detecting with a differential refractive index detector connected to a chromatograph.
- the content of the low molecular weight component having a molecular weight of 5,000 or less is preferably 10% or less and 0.5 to 6.0% from the viewpoint of doping stability. More preferred is 0.5 to 6.0%.
- Examples of a method for obtaining a polyvinyl sulfonic acid having a low molecular weight component having a molecular weight of 5,000 or less in the above range include, for example, monomer concentration, polymerization temperature, polymerization time in polymerization methods such as radical polymerization, cationic polymerization, and anionic polymerization. And a method of adjusting the polymerization initiator concentration in a timely manner.
- the content of low molecular weight components having a molecular weight of 5,000 or less can also be obtained by the GPC measurement described above.
- the polyvinyl sulfonic acid of this embodiment has an absorbance of 0.1 or more (0.2% by mass in aqueous solution, cell length 10 mm) in the wavelength range of 255 to 800 nm.
- the absorbance is preferably from 0.1 to 5.0, and more preferably from 0.1 to 2.0.
- “having an absorbance of 0.1 or more in the wavelength range of 255 to 800 nm (aqueous solution 0.2% by mass, cell length 10 mm)” means an aqueous solution having a concentration of 0.2% by mass of polyvinyl sulfonic acid.
- the absorbance when UV measurement is performed in a cell having an optical path length of 10 mm, the absorbance is 0.1 or more at an arbitrary wavelength within a wavelength range of 255 to 800 nm.
- the absorbance may be measured by fixing to an arbitrary wavelength (for example, 255 nm), or the absorbance may be measured while changing the measurement wavelength in the range of 255 to 800 nm.
- the polyvinyl sulfonic acid has multiple bonds.
- Such polyvinyl sulfonic acid can exhibit stable doping performance because the mobility of the polymer main chain is lowered.
- the polyvinyl sulfonic acid of the present embodiment has an absorbance of 0.1 or more (aqueous solution 0.2 mass%, cell length 10 mm) in the wavelength range of 475 to 575 nm.
- Polyvinylsulfonic acid having an absorbance of 0.1 or more in the wavelength range of 475 to 575 nm (aqueous solution 0.2 mass%, cell length 10 mm) is estimated to have more multiple bonds.
- “having an absorbance of 0.1 or more in the wavelength range of 475 to 575 nm (aqueous solution 0.2 mass%, cell length 10 mm)” means that the polyvinyl sulfonic acid concentration is 0.2 mass%. This means that when UV measurement is performed using a cell having an optical path length of 10 mm, the absorbance is 0.1 or more in the wavelength range of 475 to 575 nm.
- the polyvinyl sulfonic acid of the present embodiment preferably has a glass transition point of 100 ° C. or higher from the viewpoint of doping stability.
- Such polyvinyl sulfonic acid can be obtained, for example, by introducing a crosslinked structure into the molecular structure.
- the method of introducing a crosslinked structure into the molecular structure is preferably a method in which a crosslinking agent is added and reacted during polymerization, and after linear polymer polymerization, it is preferable to crosslink by applying energy to the linear polymer, such as heat, light, or electron beam. Is the method.
- the substance used as the crosslinking agent may be any monomer that is polymerized and reacted with the vinyl sulfonic acid monomer.
- cross-linking agent having multiple bonds as in the case of vinyl sulfonic acid monomers, and divinyl sulfone, divinylbenzene, 1,4-divinylcyclohexane, 1,3-butadiene and the like Compounds are mentioned as typical crosslinking agents.
- the doping stability tends to be further improved.
- Method for producing polyvinyl sulfonic acid of the present embodiment The molar amount of the sulfonic acid group derived from the vinyl sulfonic acid monomer of the present embodiment is in the specific range, and the specific absorbance is in the wavelength range of 255 to 800 nm.
- the method for producing a polyvinyl sulfonic acid having an acid content can be preferably obtained by a method for producing it with fewer steps as described below.
- the manufacturing method of the polyvinyl sulfonic acid of this Embodiment superposes the process which superposes
- the manufacturing method of the polyvinyl sulfonic acid of this Embodiment is demonstrated in detail.
- the polymer isolation step after the polymerization when the polymerization is carried out without solvent, it can be isolated as it is, and when the polymerization is carried out in the presence of a solvent, use a solvent distillation step or a reprecipitation step and a drying step.
- an alkali metal salt when used as a monomer, it can be isolated by a method including two steps of a dealkalization step and a solvent distillation step.
- the solvent is usually distilled off and / or dried at a temperature of 60 ° C. or lower.
- the polyvinyl sulfonic acid of the present embodiment can be obtained by heating the polymer isolated as described above at a temperature exceeding 60 ° C.
- the polyvinyl sulfonic acid When the polyvinyl sulfonic acid is heated at a temperature exceeding 60 ° C., the desulfonation reaction and dehydration reaction occur, thereby causing the content of sulfonic acid groups, the formation of sulfonic acid anhydride, the UV absorbance, the glass transition point, the degree of crosslinking. Etc. can be adjusted.
- the heating temperature is preferably in the range of 80 to 180 ° C, more preferably in the range of 90 to 120 ° C.
- the heating temperature is equal to or higher than the lower limit value, the reaction rate of desulfurization and dehydration reaction is high and the heat treatment time is shortened.
- the heating temperature is equal to or lower than the upper limit value, many types of reactions occur simultaneously. And the product dissolves in water, making it difficult to be in a gel state.
- this heating step is preferably carried out in the solvent distillation step or drying step of the polymer isolation step.
- the heating method can be performed using a powder dryer or a kneader, or a known method such as a microwave can be used.
- This heat treatment may be performed in a solvent. That is, in the step of desulfonation and dehydration by heating, the polyvinyl sulfonic acid is preferably in a mixture state with a solvent.
- a method of heating in a highly polar solvent typified by water, methanol, ethanol, IPA, butanol, DMSO, DMF, DMAc or the like that dissolves polyvinyl sulfonic acids, benzene, toluene, hexane, octane, etc.
- a method in which a polymer is dispersed in a low polar solvent and heated.
- the heating temperature is preferably in the range of 80 to 180 ° C, more preferably in the range of 110 to 160 ° C.
- it is preferably 80% by mass or less, more preferably 50% by mass or less, further preferably 20% by mass or less, and particularly preferably 10% by mass or less.
- the amount of solvent used should be such that it can coexist with the polyvinyl sulfonic acid polymer solid in the reaction vessel and can be heated. That's fine.
- desulfonation and dehydration can be accelerated by removing and removing sulfur oxides and water generated from polyvinyl sulfonic acid together with solvent vapor from the reactor. Is preferred.
- the heat treatment time varies depending on the heating method. When using a method that can transfer heat to the entire solid at high speed, such as microwaves, it can be processed in seconds to hours.
- the heating time in a heating system in which heat is conducted from the outside to the inside of a substance using a normal heat source is preferably 0.01 to 1000 hours. More preferably, it is 0.5 to 500 hours, and further preferably 2 to 250 hours. The heating time may be short when the heating temperature is high, and long when the heating temperature is low.
- a sulfonic anhydride from between sulfonic acid groups by the dehydration reaction by heating.
- the sulfonic anhydride may be formed by dehydration reaction within a molecule or between molecules.
- Polyvinylsulfonic acid has a cross-linked structure when intermolecular dehydration occurs, and the solubility in water may be reduced. Therefore, it is preferable to perform intermolecular dehydration within a range that can be dissolved in water.
- polyvinyl sulfonic acid having an intramolecular dehydration structure is preferable from the viewpoint that the degree of decrease in water solubility is very small.
- the composite of this embodiment includes the above-described polyvinyl sulfonic acid and a conductive polymer.
- the sulfonic acid group of the polyvinyl sulfonic acid described above interacts by doping into a conductive polymer. This interaction is considered to be an electrostatic interaction between the anion of polyvinyl sulfonic acid and the cation of the conductive polymer.
- the weight ratio of the polymer for dopant (polyvinylsulfonic acid) to the weight of the conductive polymer is preferably small, and the weight ratio is preferably 4 or less.
- the weight ratio when it is desired to suppress a decrease in conductivity even when various additives are added, the weight ratio can be further reduced and can be 1 or less.
- additives such as celluloses, silicones, amines, polyurethanes, polyesters, polyamides, polyimides, polyolefins, polyethers, poly (meth) acrylates, etc.
- An additive for improving physical properties at the time of film formation can be mentioned.
- these additives there are those that adhere to the outside of the composite particles and those that enter the inside of the composite. When such an additive adheres to the outside of the composite particle, the additive itself becomes a resistance between the particles and the electrical conductivity decreases. When the additive enters the inside of the composite, the effect of the additive itself on the particle-to-particle resistance is reduced, and a decrease in electrical conductivity is suppressed.
- Additives that can penetrate into the composite include silicones and amines that are highly compatible with the polyvinyl sulfonic acid forming the composite, and these compounds are additives that have little effect on the conductive performance. It is a very useful additive.
- additives used in dispersions containing a conductive polymer can be added.
- pigments, dyes, antifoaming agents, crosslinking agents, stabilizers, surfactants and the like can be added.
- the dispersion liquid of the present embodiment is obtained by dispersing the above composite in a solvent.
- the dispersion in which the complex is dispersed in water and / or a polar solvent is excellent in high dispersion stability and dispersibility in a solvent other than water.
- This is presumed to be because many sulfonic acid groups necessary for dispersing a highly lipophilic conductive polymer in a polar solvent are present in the polyvinyl sulfonic acid of the present embodiment. That is, in PSS, which is often used as a dopant for conductive polymers, there is a high probability that sulfonic acid groups are oriented in the same direction relative to the molecular chain, and many sulfonic acid groups are used for interaction with conductive polymers. Therefore, it is not used for interaction with a solvent for dispersion stabilization.
- the direction of the sulfonic acid group is random with respect to the molecular chain, and the sulfonic acid in the vicinity of the sulfonic acid interacting with the conductive polymer is opposite to the conductive polymer. It is presumed that this is because it can be directed to interact with the solvent to aid dispersion.
- the dispersion of this embodiment can increase the concentration of the complex.
- the concentration of the complex can be 1% by mass or more based on the total weight of the dispersion. Considering the production of a process for coating the dispersion and producing a conductive film, it is preferable to use a dispersion having a composite concentration of 5% by mass or more. Even the high-concentration dispersion can be stably present.
- the solvent is not particularly limited.
- alcohols such as methanol, ethanol, isopropanol, butanol; dimethyl ether, methyl ethyl ether, diethyl ether, Ethers such as ethyl propyl ether, dipropyl ether and ethyl butyl ether; ketones such as acetone, methyl ethyl ketone and diethyl ketone; nitriles such as acetonitrile, propionitrile and butyronitrile; esters such as ethyl acetate and butyl acetate are preferably used Is done. Even in these organic solvents, the complex of the present embodiment can be stably dispersed.
- the “dispersion” is also referred to as “water dispersion”.
- the dispersion according to the present embodiment is a dispersion for forming a conductive film, and the conductive film contains poly (3,4-ethylenedioxythiophene), and 2 ⁇ in the reflection method XDR measurement of the conductive film.
- the peak area ratio (peak K area / peak L area) between the peak K in the range of 8 ° to 10 ° and the peak L in the range of 2 ⁇ between 24 ° and 28 ° is 1.0 to 10.0. Is preferred.
- a conductive film formed from such a dispersion is preferable because of high conductivity.
- the dispersion liquid of the present embodiment preferably contains a conductive polymer and a polyanion.
- a conductive polymer for example, the conductive polymer mentioned above is mentioned, Poly (3,4-ethylene dioxythiophene) is preferable.
- a polyanion for example, the polyvinyl sulfonic acid mentioned above is preferable.
- the method for producing the dispersion according to the present embodiment is not particularly limited, but usually a polyanion (for example, the above-described polyvinyl sulfonic acid) is dissolved and / or dispersed in a solvent, and the solvent is dissolved and / or dispersed. Among them, a step of polymerizing monomers of a conductive polymer is included.
- a polyanion for example, the above-described polyvinyl sulfonic acid
- the polymerization product obtained in the polymerization step is taken out as a solid, the solid is washed, and the solid after the washing step is dissolved in a solvent. It is preferable to further include a step of dispersing.
- the monomers of the conductive polymer used may be any monomer that can produce the conductive polymer by a monomer polymerization reaction.
- the polythiophene-based conductive polymer that is particularly preferable as the conductive polymer is, for example,
- R 11 and R 12 independently represent hydrogen or an alkyl group having 1 to 5 carbon atoms, or together form an alkylene group having 1 to 5 carbon atoms. May be replaced] It is produced by homopolymerizing or copolymerizing 3,4-dioxythiophene represented by
- the amount of polyvinyl sulfonic acid during the polymerization reaction is preferably in the range of 0.5 to 50 mol, more preferably in the range of 0.8 to 10 mol, and even more preferably 1 mol per mol of the polymerization monomer.
- the range is ⁇ 4 mol.
- the solvent used in the polymerization reaction is water and / or a polar solvent, and the same solvents as those described as the solvent in the dispersion of the present embodiment can be used.
- an appropriate oxidizing agent may be used.
- persulfuric acid persulfate represented by sodium persulfate, potassium persulfate, and ammonium persulfate
- hydrogen peroxide metal oxide represented by potassium permanganate
- metal salts such as ferric nitrate and ferric nitrate. They may be used alone or in combination of two or more.
- a preferred oxidant is persulfate, and a more preferred oxidant is ammonium persulfate, which is a metal-free persulfate.
- the stirring method is not particularly limited, but an efficient stirring method is preferable, and examples include a stirring method using a paddle blade, a propeller blade, an anchor blade, a fiddler blade, a turbine blade, a max blend blade, a full zone blade, and the like.
- a high speed mixer, a homogenizer and a kneader can be used to give a high share during polymerization.
- the polymerization temperature is not particularly limited, but is usually preferably ⁇ 30 ° C. to 100 ° C. In order to suppress side reactions and decomposition reactions, the temperature is more preferably ⁇ 20 to 80 ° C., further preferably ⁇ 10 to 40 ° C.
- the time for conducting the polymerization reaction is appropriately set according to the presence or absence of the oxidizing agent, the type and amount of the oxidizing agent, the polymerization temperature, etc., but is usually about 0.5 to 100 hours, and 10 to 10 in consideration of productivity. It is preferable to carry out the polymerization under polymerization conditions of about 40 hours.
- steps other than the above polymerization reaction step may be provided.
- a purification step for removing an oxidizing agent or a low molecular weight substance can be added.
- the purification method include a dialysis method, an ion exchange method, and a centrifugal washing method, and these can be performed by one purification step or a combination of two or more.
- a more preferable method is to remove cations and anions by ion exchange, and then centrifuge.
- the composite is precipitated, the precipitate is washed, and components other than the complex dissolved and / or dispersed in the solution are removed.
- lowering the content of polyvinyl sulfonic acid decomposition products and oxidant residues leads to an improvement in the conductivity of the finally obtained conductive film and an improvement in the heat resistance of the conductive film.
- the produced dispersion can also be pulverized using a rotary homogenizer or an ultrasonic homogenizer. As a result, a dispersion having an average particle size of the dispersoid of 10 ⁇ m to 1 nm can be obtained.
- the additive is not particularly limited, and examples thereof include a compound having a water-soluble hydroxyl group, a water-soluble sulfoxide, a water-soluble amide compound, and a compound having a water-soluble lactone structure.
- the compound having a water-soluble hydroxyl group is not particularly limited, and examples thereof include polyhydric alcohols and derivatives thereof. Although it does not specifically limit as a polyhydric alcohol, For example, glycerol and ethylene glycol are mentioned.
- the polyhydric alcohol derivative is not particularly limited, and examples thereof include polyhydric alcohol monoethers such as diethylene glycol monoethyl ether.
- the water-soluble sulfoxide is not particularly limited, and examples thereof include dimethyl sulfoxide and diethyl sulfoxide.
- the water-soluble amide compound is not particularly limited, and examples thereof include N, N-dimethylformamide and N-methylpyrrolidone.
- the compound having a water-soluble lactone structure is not particularly limited, and examples thereof include ⁇ -butyrolactone and ⁇ -valerolactone.
- additives may be used alone or in combination of two or more.
- the addition amount of the additive is usually preferably 0.1 to 50% by weight, more preferably 1 to 20% by weight, based on the total weight of the dispersion.
- additives that improve physical properties during film formation of composites such as celluloses, silicones, amines, polyurethanes, polyesters, polyamides, polyimides, polyolefins, polyethers, poly (meth) acrylates, etc. May be added.
- these additives there are those that adhere to the outside of the composite particles and those that enter the inside of the composite.
- silicones and amines that are highly compatible with polyvinyl sulfonic acids that can enter the inside of the composite are electrically conductive. This additive is very useful as an additive having little influence on performance.
- additives used in dispersions containing a conductive polymer can be added.
- pigments, dyes, antifoaming agents, crosslinking agents, stabilizers, surfactants and the like can be added.
- the blending amount of these additives can be appropriately set within the range where the effects of the present embodiment are exhibited.
- the conductive film of the present embodiment is a conductive film manufactured using the above dispersion.
- the above dispersion liquid can be applied to a substrate to form a film, thereby forming a conductive film.
- a conductive film including a composite of the above-described polyvinyl sulfonic acids and a conductive polymer is provided.
- the film forming method is not particularly limited.
- a casting method or a spin coating method a micro gravure coating method, a gravure coating method, a bar coating method, a roll coating method, a wire bar coating method, a dip coating method, a spray coating method, Examples thereof include screen printing, flexographic printing, offset printing, and inkjet printing.
- a base material for example, a plastic substrate, a nonwoven fabric, a glass substrate, a silicon substrate etc. are mentioned. They may be coated with ITO, tin oxide, indium oxide or the like.
- the shape of the substrate may be a sheet shape, a film shape, a plate shape, a disk shape, or the like.
- the plastic is not particularly limited.
- polyester resins polystyrene resins, polyolefin resins such as polyethylene and polypropylene, polyimide resins, polyamide resins, polysulfone resins, polycarbonate resins, polyvinyl chloride resins, Examples thereof include phenolic resins and epoxy resins. These may be homopolymers or copolymers. Moreover, these may be used individually by 1 type and may be used in mixture of 2 or more types.
- the drying conditions for coating the dispersion on the substrate to form a film are, for example, 20 to 250 ° C. and 5 seconds to 5 weeks.
- the thickness of the conductive film of this embodiment is appropriately set depending on the application, but is preferably 1 nm to 20 ⁇ m, and more preferably about 2 nm to 500 nm.
- the conductive film of this embodiment can be evaluated for crystallinity of a complex of a conductive polymer and a polyanion by XRD measurement.
- the insulating component is a component derived from the raw material dissolved in the dispersion, that is, a monomer of conductive polymer, polyvinyl sulfonic acid, an oxidizing agent, and an oxidizing agent residue.
- the conductive film of the present embodiment is manufactured using, for example, a dispersion liquid in which a composite containing the above-described decoy conductive polymer and polyvinyl sulfonic acid is dispersed in a solvent.
- the conductive film thus manufactured has a specific peak area ratio in XRD measurement.
- the conductive film manufactured as described above has a peak K of 2 ⁇ ranging from 8 ° to 10 ° and a peak L of 2 ⁇ ranging from 24 ° to 28 ° in the reflection XRD measurement method.
- the area ratio (area of peak K / area of peak L) is 1.0 to 10.0.
- the peak area ratio (peak K area / peak L area) is preferably 1.2 to 8.0, and more preferably 2.0 to 5.2.
- the present inventors have found that the conductive film of the conductive film has a certain conductivity because the peak area ratio in the XRD measurement, which is a factor that determines the polymer-polymer distance in the conductive polymer crystal that governs the conductivity, is in a specific range. I found that the rate would increase.
- a clear peak is not confirmed in the range of 2 ⁇ of 8 ° to 10 °.
- the PEDOT single crystal has no peak in the range of 2 ⁇ of 8 ° to 10 °.
- PEDOT using monomer styrene sulfonic acid as a dopant a peak of diffraction angle is confirmed in the vicinity of the angle.
- the reflection method XRD measurement method is a measurement method described in the examples described later.
- the diffraction angle 2 ⁇ is preferably in the range of 8 ° to 10 °, and the smaller the distance, the shorter the distance between the conductive polymer and the conductive polymer.
- the diffraction angle 2 ⁇ is smaller than 8 °, there is a problem that the abundance of sulfonic acid that should be present between the conductive and conductive molecules is lowered, the dope state is weakened, and the conductivity is lowered.
- the peak area ratio (peak K area / peak L area) of the peak K in the range 2 ⁇ of 8 ° to 10 ° and the peak L in the range 2 ⁇ of 24 ° to 28 ° is 1.0 to 10.
- the conductive polymer that can form a conductive film of 0 is not particularly limited, but a polymer having a structure in which double bonds and single bonds are alternately long in the polymer structure is preferable.
- the polymer is not particularly limited, and examples thereof include poly (p-phenylene), poly (o-phenylene), poly (m-phenylene), poly (2,6-naphthalene), and poly (9,10-anthracene).
- the alkyl group may be linear or branched, and is not particularly limited, and examples thereof include a methyl group, an ethyl group, and a propyl group.
- the alkylene group is not particularly limited, and examples thereof include a methylene group, an ethylene group, and a propylene group.
- the substituent that the alkylene group may have is not particularly limited, and examples thereof include a methyl group, an ethyl group, a hydroxymethyl group, and a hydroxyethyl group.
- the conductive film of the present embodiment contains poly (3,4-ethylenedioxythiophene), and in the reflection XDR measurement, 2K is in the range of 8 ° to 10 ° and 2 ⁇ is in the range of 24 ° to 28 °.
- the ratio of the peak area to the peak L is preferably 1.0 to 10.0.
- the peak area ratio (peak K area / peak L area) between the peak K in the range of 2 ⁇ of 8 ° to 10 ° and the peak L of 2 ⁇ in the range of 24 ° to 28 ° is 1.0 to 10.
- the polyvinyl sulfonic acid capable of forming a conductive film of 0.0 is not particularly limited, but a sulfonic acid monomer having an aromatic ring between the polymer main chain and the sulfonic acid group (hereinafter referred to as “containing side chain aromatic ring”). Those having a low content of “sulfonic acid monomer” are also preferred.
- a preferable polyvinyl sulfonic acid capable of forming the conductive film as described above is a polyvinyl sulfonic acid containing a monomer unit derived from a vinyl sulfonic acid monomer represented by the following general formula (1) ′.
- R 1 , R 2 and R 3 are each independently hydrogen, an alkyl group having 1 to 15 carbon atoms or an alkylene group, and Z is hydrogen, halogen, an alkyl group having 1 to 15 carbon atoms or An alkylene group, a metal ion, an ammonium ion, a protonated primary, secondary or tertiary amine, or a quaternary ammonium ion]
- the vinyl sulfonic acid monomer represented by the general formula (1) ′ is not particularly limited, and examples thereof include alkyl-substituted vinyl such as 1-alkyl vinyl sulfonic acid, 2-alkyl vinyl sulfonic acid, and 1,2-alkyl sulfonic acid.
- Sulfonic acid Sodium vinyl sulfonate, sodium 1-alkylvinyl sulfonate, potassium vinyl sulfonate, ammonium vinyl sulfonate, vinyl sulfonic acid alkyl amine salt, etc .; sulfone such as vinyl sulfonic acid fluoride, vinyl sulfonic acid chloride, etc.
- Acid halides; vinyl sulfonic acid and the like are typical vinyl sulfonic acid monomers.
- vinyl sulfonates and vinyl sulfonates in which R 1 , R 2 , and R 3 are hydrogen and Z is hydrogen, sodium, or potassium are preferable monomers.
- More preferable polyvinyl sulfonic acid is 50.0 to 98.0 mol% of the molar amount of the sulfonic acid group derived from the vinyl sulfonic acid monomer represented by the general formula (1) ′ with respect to the molar amount of all the monomer units in the polymer. It is the polyvinyl sulfonic acid made into the range.
- the sulfonic acid group includes an anhydride obtained by dehydration condensation of two molecules of sulfonic acid.
- Polyvinylsulfonic acid containing an anhydride that has been heat-treated and dehydrated and condensed with two molecules of sulfonic acid groups simultaneously with desulfonation is a preferred polymer.
- the electrically conductive film of this Embodiment is manufactured using said dispersion liquid, and can be provided with high electrical conductivity and low surface resistivity.
- the range of electrical conductivity and surface resistivity is set according to the application, but according to the present embodiment, the value of electrical conductivity is preferably 0.01 to 1,000 Scm ⁇ 1 , particularly preferably 0. a .1 ⁇ 500Scm -1, is preferably a surface resistivity can be obtained 100,000 ⁇ 5 ⁇ / ⁇ , particularly preferably 200 ⁇ 10 ⁇ / ⁇ conductive film.
- the polyvinyl sulfonic acid constituting the conductive film of the present embodiment has many sulfonic acid groups facing the substrate. Therefore, the conductive film of this embodiment also has good substrate adhesion.
- the conductive film of the present embodiment can be used in various optoelectronic component applications. Examples include applications that require particularly good conductivity, capacitors, conductive films, conductive sheets, and the like. Specific examples include polymer light-emitting diodes, organic solar power generation, secondary batteries, and conductive polymer sensors. , Thin film transistor elements, electroluminescent elements, electrolytic capacitors, and the like. It can also be used as an alternative to the ITO thin film.
- the measurement conditions of the apparatus were a column temperature of 40 ° C. and a flow rate of 1.0 ml / min.
- a 0.2M sodium nitrate aqueous solution was used as an eluent.
- GPL measurement of each polymer was performed by injecting 20 ⁇ l of an analytical sample diluted to 2% by weight with the eluent and detecting it with a differential refractive index detector connected to the chromatograph.
- the content (%) of vinyl sulfonic acid remaining in each polymer is defined as follows.
- the total area corresponding to the solute in the chromatogram is A.
- the area corresponding to the acid was B, it was calculated by the following formula.
- the content (%) of a low molecular weight component having a molecular weight of 5000 or less in each polymer is defined as A in the chromatogram obtained by measuring the analytical sample with the apparatus, and the total area corresponding to the solute in the chromatogram is A.
- the total area C corresponding to the solute after the elution time corresponding to a molecular weight of 5000 was used, the calculation was performed by the following formula.
- the content (ppm) of polyvinyl sulfonic acid dissolved in each dispersion was determined as follows. First, in the chromatogram obtained by measuring the analytical sample with the apparatus, the area corresponding to the solute in the chromatogram was obtained. Next, the content corresponding to the obtained area was determined from a calibration curve obtained from a chromatogram having a known content, and the content was defined as the content of polyvinyl sulfonic acid.
- the unit of the molar concentration of the titrant is mol / L
- V is the titration amount (mL) of the titrant
- 108 is the molecular weight (g / mol) of vinyl sulfonic acid.
- W is the mass (g) of the polymer solid sample
- f is the calibration factor of the titrant.
- the surface resistivity of the prepared conductive film was measured by a four-probe method using a Lorester GP (MCP-T610) manufactured by Mitsubishi Chemical Analytech Co., Ltd. Further, the film thickness of the prepared conductive film was measured using a Digimatic Indicator ID-C112CX manufactured by Mitutoyo Corporation. After the measurement, the electrical conductivity of the conductive film was calculated by the following formula (2).
- ⁇ is the surface resistivity ( ⁇ / ⁇ )
- t is the film thickness (cm).
- peak separation was performed by the following method.
- I is strength
- A, B, and C are constants
- the peak area ratio E between the peak K with 2 ⁇ ranging from 8 ° to 10 ° and the peak L with 2 ⁇ ranging from 24 ° to 28 ° was determined by the following equation.
- ⁇ Particle size measurement> The average particle size of the dispersoid in each dispersion was measured using FPAR-1000 manufactured by Otsuka Electronics under the following conditions. Measurement sample: a dispersion diluted 50 times with ion-exchanged water. Measuring probe: Dilute probe. Particle size analysis: MARQUARDT method.
- the heat resistance test of the conductive film in this example was performed as follows. First, the dispersion was spin-coated on a 25 ⁇ 25 mm slide glass and dried at 100 ° C. for 30 minutes to form a conductive film. The conductive film was placed in a small high temperature chamber manufactured by ESPEC CORP. And heated at 135 ° C. for 55 hours. The surface resistance value of the conductive film before and after the heating was measured by a four-probe method using a Lorester GP (MCP-T610) manufactured by Mitsubishi Chemical Analytech Co., Ltd. The rate of increase in surface resistivity due to heating of the conductive film was determined by the following equation.
- Solid state NMR measurement The solid state NMR measurement of polyvinyl sulfonic acid in this example was performed using ECA700 manufactured by JEOL under the following conditions. Measurement nucleus: 13 C. Measuring method: CP / MAS method. Observation frequency: 176.05 MHz. Analysis sample tube: 4 mm ⁇ NMR tube. MAS: 10 kHz. Integration count: 1000 times.
- the solid state NMR measurement of the conductive film in the present example was performed under the above conditions except that the analytical sample was previously mixed with 7 times the amount of KBr and placed in the NMR tube, and the cumulative number was 12,000. The measurement was performed in the same manner as above.
- radical polymerization initiator 2,2′-azobis (2-methylpropionamidine) dihydrochloride manufactured by Wako Pure Chemical Industries, Ltd., hereinafter also referred to as “V-50”
- V-50 radical polymerization initiator 2,2′-azobis (2-methylpropionamidine) dihydrochloride
- the aqueous solution in the flask was stirred at 10 ° C. for 27 hours to obtain a polymerization solution.
- tetrahydrofuran was used as a reprecipitation solvent, and reprecipitation refinement
- purification was repeated until residual VSA became 1% or less, and polyvinylsulfonic acid (PVS) aqueous solution was obtained.
- PVS polyvinylsulfonic acid
- the obtained polymerization liquid was mixed with 917.74 g of ion-exchanged water to prepare a 5.7 wt% aqueous potassium polyvinyl sulfonate solution.
- a column tower (inner diameter: 50 mm, height: 600 mm) packed with 400 mL of a strongly acidic ion exchange resin (DOWEX (registered trademark) Monosphere 650C) regenerated with hydrochloric acid in advance was charged with the prepared polyvinyl potassium sulfonate aqueous solution at a rate of 200 mL / hour.
- DOWEX registered trademark
- Monosphere 650C a strongly acidic ion exchange resin
- aqueous solution in the flask was stirred at 40 ° C. for 45 hours for polymerization to obtain a polymerization solution.
- the obtained polymerization solution was mixed with 522 g of ion-exchanged water to prepare a 5.6% by weight aqueous sodium polyvinyl sulfonate solution.
- Example 1 The PVS aqueous solution obtained in Production Example 1 was heated and vacuum dried at 50 ° C. for 72 hours to obtain a PVS solid. The water content of the obtained PVS solid was 13.5% by weight. 2 g of this PVS solid was placed in a 100 mL beaker and heat-treated with a blow dryer at 110 ° C. for 10 hours. The heat-treated PVS was subjected to GPC measurement, absorbance measurement, and measurement of the molar amount of the sulfonic acid group as described above. The results are shown in Table 1.
- Example 2 Using the PVS aqueous solution obtained in Production Example 2, the heat treatment time after obtaining the PVS solid was changed to 1 hour, the same operation as in Example 1 was carried out, and the heat-treated PVS, poly (3, An aqueous dispersion of a composite of 4-ethylenedioxythiophene) and polyvinyl sulfonic acid and a conductive film were obtained.
- Example 3 Except that the heat treatment time after obtaining the PVS solid was 5 hours, the same operation as in Example 2 was performed, and the heat-treated PVS, poly (3,4-ethylenedioxythiophene), polyvinyl sulfonic acid, An aqueous dispersion of the composite and a conductive film were obtained.
- Example 4 Except that the heat treatment time after obtaining the PVS solid was 7.5 hours, the same operation as in Example 2 was performed, and the heat treated PVS, poly (3,4-ethylenedioxythiophene) and polyvinylsulfone An aqueous dispersion of a complex with an acid and a conductive film were obtained.
- Example 5 Except that the heat treatment time after obtaining the PVS solid was 10 hours, the same operation as in Example 2 was performed, and the heat-treated PVS, poly (3,4-ethylenedioxythiophene), polyvinylsulfonic acid, An aqueous dispersion of the composite and a conductive film were obtained.
- Example 6 Except that the heat treatment time after obtaining the PVS solid was 12.5 hours, the same operation as in Example 2 was carried out, and the heat-treated PVS, poly (3,4-ethylenedioxythiophene) and polyvinylsulfone An aqueous dispersion of a complex with an acid and a conductive film were obtained.
- Example 7 Except that the heat treatment time after obtaining the PVS solid was set to 15 hours, the same operation as in Example 2 was performed, and the heat-treated PVS, poly (3,4-ethylenedioxythiophene), polyvinyl sulfonic acid, An aqueous dispersion of the composite and a conductive film were obtained.
- Example 8 The heat treatment temperature after obtaining the PVS solid was set to 100 ° C., and the heat treatment time was set to 48 hours. The same operation as in Example 2 was performed, and the heat-treated PVS, poly (3,4-ethylenedioxide) was subjected to heat treatment. An aqueous dispersion of a composite of oxythiophene) and polyvinyl sulfonic acid, and a conductive film were obtained.
- Example 9 The heat treatment temperature after obtaining the PVS solid was set to 100 ° C., and the heat treatment time was set to 72 hours. An aqueous dispersion of a composite of oxythiophene) and polyvinyl sulfonic acid, and a conductive film were obtained.
- Example 10 The heat treatment temperature after obtaining the PVS solid was 95 ° C., and the heat treatment time was 24 hours. The same operation as in Example 2 was performed, and the heat-treated PVS, poly (3,4-ethylenedibenzene) was treated. An aqueous dispersion of a composite of oxythiophene) and polyvinyl sulfonic acid, and a conductive film were obtained.
- Example 11 The heat treatment temperature after obtaining the PVS solid was 95 ° C., and the heat treatment time was 72 hours. The same operation as in Example 2 was performed, and the heat-treated PVS, poly (3,4-ethylenedioxide) was treated. An aqueous dispersion of a composite of oxythiophene) and polyvinyl sulfonic acid, and a conductive film were obtained.
- Example 12 The heat treatment temperature after obtaining the PVS solid was set to 95 ° C., and the heat treatment time was set to 96 hours. An aqueous dispersion of a composite of oxythiophene) and polyvinyl sulfonic acid, and a conductive film were obtained.
- Example 13 Except that the heat treatment temperature after obtaining the PVS solid was 95 ° C. and the heat treatment time was 120 hours, the same operation as in Example 2 was carried out, and the heat-treated PVS, poly (3,4-ethylenedioxide) was treated. An aqueous dispersion of a composite of oxythiophene) and polyvinyl sulfonic acid, and a conductive film were obtained.
- Example 14 Except that the heat treatment temperature after obtaining the PVS solid was 95 ° C. and the heat treatment time was 144 hours, the same operation as in Example 2 was carried out, and the heat-treated PVS, poly (3,4-ethylenedioxide) was treated. An aqueous dispersion of a composite of oxythiophene) and polyvinyl sulfonic acid, and a conductive film were obtained.
- Example 15 The heat treatment temperature after obtaining the PVS solid was 95 ° C., and the heat treatment time was 192 hours. The same operation as in Example 2 was performed, and the heat treated PVS, poly (3,4-ethylenedioxide) was treated. An aqueous dispersion of a composite of oxythiophene) and polyvinyl sulfonic acid, and a conductive film were obtained.
- Example 16 The heat treatment temperature after obtaining the PVS solid was 95 ° C., and the heat treatment time was 240 hours. The same operation as in Example 2 was performed, and the heat-treated PVS, poly (3,4-ethylenedioxide) was treated. An aqueous dispersion of a composite of oxythiophene) and polyvinyl sulfonic acid, and a conductive film were obtained.
- Example 17 Using the PVS aqueous solution obtained in Production Example 3, the heat treatment temperature after obtaining the PVS solid was 115 ° C., and the heat treatment time was 1 hour. An aqueous dispersion of a composite of treated PVS, poly (3,4-ethylenedioxythiophene) and polyvinyl sulfonic acid, and a conductive film were obtained.
- Example 18 Except that the heat treatment time after obtaining the PVS solid was 2 hours, the same operation as in Example 17 was performed, and the heat-treated PVS, poly (3,4-ethylenedioxythiophene), polyvinylsulfonic acid, An aqueous dispersion of the composite and a conductive film were obtained.
- Example 19 Except that the heat treatment time after obtaining the PVS solid was 4 hours, the same operation as in Example 17 was performed, and the heat-treated PVS, poly (3,4-ethylenedioxythiophene), polyvinyl sulfonic acid, An aqueous dispersion of the composite and a conductive film were obtained.
- Example 20 The heat treatment temperature after obtaining the PVS solid was set to 110 ° C., and the heat treatment time was set to 3 hours. An aqueous dispersion of a composite of oxythiophene) and polyvinyl sulfonic acid, and a conductive film were obtained.
- Example 21 The heat treatment temperature after obtaining the PVS solid was 110 ° C., and the heat treatment time was 4 hours. The same operation as in Example 17 was performed, and the heat-treated PVS, poly (3,4-ethylenedibenzene) was treated. An aqueous dispersion of a composite of oxythiophene) and polyvinyl sulfonic acid was obtained.
- Example 22 The heat treatment temperature after obtaining the PVS solid was 110 ° C., and the heat treatment time was 5 hours. The same operation as in Example 17 was performed, and the heat-treated PVS, poly (3,4-ethylenedioxide) was treated. An aqueous dispersion of a composite of oxythiophene) and polyvinyl sulfonic acid, and a conductive film were obtained.
- Example 23 The heat treatment temperature after obtaining the PVS solid was 110 ° C., and the heat treatment time was 7.5 hours. The same operation as in Example 17 was performed, and the heat treated PVS and poly (3,4- An aqueous dispersion of a composite of ethylenedioxythiophene) and polyvinyl sulfonic acid and a conductive film were obtained.
- Example 24 The heat treatment temperature after obtaining the PVS solid was set to 110 ° C., and the heat treatment time was set to 10 hours. An aqueous dispersion of a composite of oxythiophene) and polyvinyl sulfonic acid, and a conductive film were obtained.
- Example 25 The heat treatment temperature after obtaining the PVS solid was 100 ° C., and the heat treatment time was 72 hours. The same operation as in Example 17 was performed, and the heat-treated PVS, poly (3,4-ethylenedibenzene) was treated. An aqueous dispersion of a composite of oxythiophene) and polyvinyl sulfonic acid, and a conductive film were obtained.
- Example 1 The same operation as in Example 1 was performed except that the heat treatment after obtaining the PVS solid was not performed. A precipitate was generated in the obtained aqueous dispersion.
- Example 2 The same operation as in Example 2 was performed except that the heat treatment after obtaining the PVS solid was not performed. A precipitate was generated in the obtained aqueous dispersion.
- Example 3 The same operation as in Example 17 was performed except that the heat treatment after obtaining the PVS solid was not performed. A precipitate was generated in the obtained aqueous dispersion.
- Example 26 An aqueous dispersion of a composite of poly (3,4-ethylenedioxythiophene) and polyvinylsulfonic acid was carried out in the same manner as in Example 10 except that the amount of heat-treated PVS was changed to 0.4 g. Got. This aqueous dispersion was stable and did not cause precipitation. Moreover, the electrical conductivity of the electrically conductive film obtained from this water dispersion was 5 S / cm. The weight ratio of the other components to the conductive polymer component calculated from the charged ratio was 2.0.
- Example 27 An aqueous dispersion of a composite of poly (3,4-ethylenedioxythiophene) and polyvinylsulfonic acid was carried out in the same manner as in Example 10 except that the amount of heat-treated PVS was changed to 0.8 g. Got. This aqueous dispersion was stable and did not cause precipitation. Moreover, the electrical conductivity of the electrically conductive film obtained from this water dispersion was 20 S / cm. The weight ratio of the other components to the conductive polymer component calculated from the charged ratio was 4.0.
- Example 28 An aqueous dispersion of a composite of poly (3,4-ethylenedioxythiophene) and polyvinylsulfonic acid was carried out in the same manner as in Example 11 except that the amount of heat-treated PVS was changed to 0.4 g. Got. This aqueous dispersion was stable and did not cause precipitation. Moreover, the electrical conductivity of the electrically conductive film obtained from this water dispersion was 23 S / cm. The weight ratio of the other components to the conductive polymer component calculated from the charged ratio was 2.0.
- Example 29 An aqueous dispersion of a complex of poly (3,4-ethylenedioxythiophene) and polyvinylsulfonic acid was carried out in the same manner as in Example 11 except that the amount of heat-treated PVS was changed to 0.8 g. Got. This aqueous dispersion was stable and did not cause precipitation. Moreover, the electrical conductivity of the electrically conductive film obtained from this water dispersion was 29 S / cm. The weight ratio of the other components to the conductive polymer component calculated from the charged ratio was 4.0.
- Example 30 An aqueous dispersion of a composite of poly (3,4-ethylenedioxythiophene) and polyvinyl sulfonic acid was carried out in the same manner as in Example 13 except that the amount of heat-treated PVS was changed to 0.4 g. Got. This aqueous dispersion was stable and did not cause precipitation. Moreover, the electrical conductivity of the electrically conductive film obtained from this water dispersion was 33 S / cm. The weight ratio of the other components to the conductive polymer component calculated from the charged ratio was 2.0.
- Example 31 An aqueous dispersion of a composite of poly (3,4-ethylenedioxythiophene) and polyvinylsulfonic acid was carried out in the same manner as in Example 13, except that the amount of heat-treated PVS was changed to 0.8 g. Got. This aqueous dispersion was stable and did not cause precipitation. Moreover, the electrical conductivity of the electrically conductive film obtained from this water dispersion was 16 S / cm. The weight ratio of the other components to the conductive polymer component calculated from the charged ratio was 4.0.
- Example 32 An aqueous dispersion of a composite of poly (3,4-ethylenedioxythiophene) and polyvinylsulfonic acid was carried out in the same manner as in Example 14 except that the amount of heat-treated PVS was changed to 0.2 g. Got. This aqueous dispersion was stable and did not cause precipitation. The electric conductivity of the conductive film obtained from this aqueous dispersion was 22 S / cm. The weight ratio of the other components to the conductive polymer component calculated from the charged ratio was 1.0.
- Comparative Example 6 Poly (3,4-ethylenedioxythiophene) and polystyrene were carried out in the same manner as in Comparative Example 5 except that the amount of PSS aqueous solution was 2.22 g and the amount of ion-exchanged water was 37.08 g. An aqueous dispersion of a complex with sulfonic acid was obtained. The electric conductivity of the conductive film obtained from this aqueous dispersion was 3.2 S / cm. The weight ratio of the other components to the conductive polymer component calculated from the charged ratio was 2.0.
- Comparative Example 7 The same operation as in Comparative Example 5 was performed except that the amount of the PSS aqueous solution was 3.33 g and the amount of ion-exchanged water was 35.97 g. Poly (3,4-ethylenedioxythiophene) and polystyrene An aqueous dispersion of a complex with sulfonic acid was obtained. The electric conductivity of the conductive film obtained from this aqueous dispersion was 4.3 S / cm. The weight ratio of the other components to the conductive polymer component calculated from the charged ratio was 3.0.
- Comparative Example 8 Poly (3,4-ethylenedioxythiophene) and polystyrene sulfone were carried out in the same manner as in Comparative Example 5 except that the amount of the PSS aqueous solution was 4.44 g and the amount of ion-exchanged water was 34.86 g. An aqueous dispersion of a complex with acid was obtained. The electric conductivity of the conductive film obtained from this aqueous dispersion was 3.2 S / cm. The weight ratio of the other components to the conductive polymer component calculated from the charged ratio was 4.0.
- Example 25-1 Using the PVS aqueous solution obtained in Production Example 2, the same heat treatment as in Example 1 was carried out except that the heat treatment temperature after obtaining the PVS solid was 130 ° C. and the heat treatment time was 1 hour. An aqueous dispersion of a composite of PVS, poly (3,4-ethylenedioxythiophene) and polyvinyl sulfonic acid, and a conductive film were obtained. Various analysis results of heat-treated PVS (dopant), evaluation results of aqueous dispersions of composites of poly (3,4-ethylenedioxythiophene) and polyvinyl sulfonic acid, and measurement of electrical conductivity and XRD of conductive film The results are shown in Table 1-1.
- Example 25-2 Using the PVS aqueous solution obtained in Production Example 2, the same heat treatment as in Example 1 was carried out except that the heat treatment temperature after obtaining the PVS solid was 150 ° C. and the heat treatment time was 1 hour. An aqueous dispersion of a composite of PVS, poly (3,4-ethylenedioxythiophene) and polyvinyl sulfonic acid, and a conductive film were obtained. Various analysis results of heat-treated PVS (dopant), evaluation results of aqueous dispersions of composites of poly (3,4-ethylenedioxythiophene) and polyvinyl sulfonic acid, and measurement of electrical conductivity and XRD of conductive film The results are shown in Table 1-1.
- Example 25-3 The PVS aqueous solution obtained in Production Example 3 was vacuum dried by heating at 50 ° C. for 72 hours to obtain a PVS solid. Thereafter, 2 g of this PVS solid was charged in a 100 mL beaker and heat-treated with a blow dryer at 90 ° C. for 480 hours. The heat-treated PVS was subjected to GPC measurement, absorbance measurement, and measurement of the molar amount of the sulfonic acid group as described above. The results are shown in Table 1-1.
- Example 25-4 The PVS aqueous solution obtained in Production Example 2 was heated and vacuum dried at 50 ° C. for 72 hours to obtain a PVS solid. Thereafter, 100 g of this PVS solid was placed in a 2000 mL separable flask, and 1200 g of toluene was added to obtain a solution. The obtained solution was heated at 110 ° C. for 8 hours in an apparatus equipped with Dean Stark, Dimroth, and a stirring blade. Thereafter, the solution was cooled, decanted with toluene, and dried under reduced pressure at 50 ° C. and 2 torr to obtain a PVS solid.
- the heat-treated PVS aqueous solution 645.2g (18.0g as PVS, 627.2g as water) is put into a 2000mL separable flask, ion-exchange water 534.7g is added, 6.0g of EDOT, ammonium persulfate (Sigma-Aldrich) 14.5 gg) was added, and the mixture was stirred and mixed at 0 ° C. for 41 hours to conduct oxidative polymerization. Next, 200 g of a cation exchange resin and 200 g of an anion exchange resin were added to this reaction mixture, and the mixture was stirred and mixed at 20 ° C.
- aqueous dispersion of a composite with was obtained.
- the stability of the obtained aqueous dispersion was evaluated as described above.
- the results are shown in Table 1-1.
- the electrically conductive film was created as mentioned above from this water dispersion, and the electrical conductivity and XRD of this electrically conductive film were measured.
- the results are shown in Table 1-1.
- the average particle diameter of the dispersoid in the dispersion and the concentration of PVS dissolved in the dispersion were measured as described above. The average particle size was 890 nm and the PVS concentration was 1400 ppm.
- the conductive film obtained from the dispersion was subjected to a heat resistance test as described above.
- the surface resistivity before heating was 2.0 ⁇ 10 3 ⁇ / ⁇
- the surface resistivity after heating was 1.0 ⁇ 10 4 ⁇ / ⁇
- the increase rate of the surface resistivity was 4.0.
- a conductive film was prepared as described above using the dispersion obtained by this centrifugal redispersion operation, and the electrical conductivity and XRD of the conductive film were measured. The results are shown in Table 1-2.
- the conductive film obtained from the dispersion was subjected to a heat resistance test as described above.
- the surface resistivity before heating was 1.5 ⁇ 10 3 ⁇ / ⁇
- the surface resistivity after heating was 5.3 ⁇ 10 3 ⁇ / ⁇
- the increase rate of the surface resistivity was 2.5.
- the dispersion obtained by the centrifugal redispersion operation was processed using a homogenizer, and the dispersoid in the dispersion was made fine.
- a conductive film was prepared as described above, and the electrical conductivity and XRD of the conductive film were measured. The results are shown in Table 1-2. Further, when the average particle size of the dispersoid in the dispersion was measured as described above, the average particle size was 190 nm.
- Example 25-5 The PVS aqueous solution obtained in Production Example 2 was heated and vacuum dried at 50 ° C. for 72 hours to obtain a PVS solid. Thereafter, 100 g of this PVS solid was placed in a 2000 mL separable flask, and 1200 g of toluene was added to obtain a solution. The obtained solution was heated at 110 ° C. for 8 hours in an apparatus equipped with Dean Stark, Dimroth, and a stirring blade. Thereafter, the solution was cooled, decanted with toluene, and dried under reduced pressure at 50 ° C. and 2 torr to obtain a PVS solid.
- aqueous dispersion of a composite with was obtained.
- the stability of the obtained aqueous dispersion was evaluated as described above.
- the results are shown in Table 1-1.
- the electrically conductive film was created as mentioned above from this water dispersion, and the electrical conductivity and XRD of this electrically conductive film were measured.
- the results are shown in Table 1-1.
- the average particle diameter of the dispersoid in the dispersion and the concentration of PVS dissolved in the dispersion were measured as described above. The average particle size was 980 nm, and the PVS concentration was 890 ppm.
- the dispersion obtained by the centrifugal redispersion operation was processed using a homogenizer, and the dispersoid in the dispersion was made into fine particles.
- a conductive film was prepared as described above, and the electrical conductivity and XRD of the conductive film were measured. The results are shown in Table 1-2. Further, when the average particle size of the dispersoid in the dispersion was measured as described above, the average particle size was 350 nm.
- the conductive film portion was crushed into powder and solid NMR was measured as described above. The measurement chart is shown in FIG. In the solid-state NMR chart shown in FIG.
- the peak near 33 ppm is the methylene carbon of PVS
- the peak near 55 ppm is the carbon to which the sulfo group of PVS is bonded
- the peak near 68 ppm is the —O—CH 2 —CH 2 — of PEDOT. It can be attributed to carbon of the O-part.
- the carbon in the thiophene ring part of PEDOT has paramagnetism by doping, and no peak is observed in the solid state NMR chart. Am. Chem. Soc. 125, 15151-15162 (2003).
- Comparative Example 11 The same evaluation as Comparative Example 10 was performed except that the dispersion was changed to PEDOT / PSS dispersion (trade name PH500) manufactured by Heraeus. The evaluation results are shown in Table 1-3.
- Comparative Example 12 The same evaluation as Comparative Example 10 was performed except that the dispersion was changed to PEDOT / PSS dispersion (trade name PH1000) manufactured by Heraeus. The evaluation results are shown in Table 1-3.
- Example 33 Using the PVS aqueous solution obtained in Production Example 5, the heat treatment time after obtaining the PVS solid was changed to 5 hours, the same operation as in Example 1 was carried out, and the heat-treated PVS, poly (3, An aqueous dispersion of a composite of 4-ethylenedioxythiophene) and polyvinyl sulfonic acid and a conductive film were obtained.
- the absorbance of the heat-treated PVS was 0.533 at 255 nm, 0.264 at 525 nm, 0.023 at 800 nm, and the molar amount of the sulfonic acid group was 96.2 mol%. This dispersion was stable and did not cause precipitation, and the electrical conductivity of the conductive film obtained from this dispersion was 35 S / cm.
- Example 34 A composite of PVS, poly (3,4-ethylenedioxythiophene) and polyvinylsulfonic acid, which was subjected to the same operation as in Example 1 except that the PVS aqueous solution obtained in Production Example 6 was used. An aqueous dispersion and a conductive film were obtained.
- the absorbance of the heat-treated PVS was 1.210 at 255 nm, 0.612 at 525 nm, 0.209 at 800 nm, and the molar amount of the sulfonic acid group was 89.5 mol%. This dispersion was stable and did not cause precipitation, and the electrical conductivity of the conductive film obtained from this dispersion was 32 S / cm.
- Example 35 The PVS aqueous solution obtained in Production Example 2 was heated and vacuum dried at 50 ° C. for 72 hours to obtain a PVS solid. 20 g of the obtained PVS solid was placed in a 300 mL beaker, and heat treatment with a blow dryer was performed at 110 ° C. for 10 hours. The absorbances of the heat-treated PVS at 255, 525, and 800 nm were 0.988, 0.332, and 0.165, respectively, and the molar amount of the sulfonic acid group was 86.5 mol%.
- This aqueous dispersion was diluted with ion exchange water to prepare a solid content of 0.7% by weight (dispersion A).
- the dispersion A was stable and did not precipitate, and the electrical conductivity of the conductive film obtained from the dispersion A was 16 S / cm.
- the weight ratio of the other components to the conductive polymer component calculated from the charged ratio was 3.0.
- Example 36 A mixed solution of 2.05 g of tetraethoxysilane (manufactured by Tokyo Chemical Industry Co., Ltd., hereinafter also referred to as “TEOS”) and 2.31 g of ethanol (manufactured by Sigma Aldrich) (TEOS is 47% by weight from the mixing ratio, hereinafter “TEOS ethanol”). 0.08 g of a “prepared solution”) was weighed in a 20 mL glass container, 15 g of the dispersion A obtained in Example 35 was added, and the mixture was stirred at room temperature for 20 hours to obtain a dispersion. This dispersion was stable and did not cause precipitation, and the electrical conductivity of the conductive film obtained from this dispersion was 12 S / cm. The weight ratio of the other components to the conductive polymer component calculated from the charged ratio was 4.4.
- Example 37 A dispersion was obtained by carrying out the same operations as in Example 36 except that the amount of the TEOS ethanol preparation liquid was changed to 0.12 g. This dispersion was stable and did not cause precipitation, and the electrical conductivity of the conductive film obtained from this dispersion was 13 S / cm. The weight ratio of the other components to the conductive polymer component calculated from the charged ratio was 5.1.
- Example 38 A dispersion was obtained by carrying out the same operations as in Example 36 except that the amount of the TEOS ethanol preparation liquid was changed to 0.22 g. This dispersion was stable and did not cause precipitation, and the electrical conductivity of the conductive film obtained from this dispersion was 11 S / cm. The weight ratio of the other components to the conductive polymer component calculated from the charged ratio was 6.9.
- Example 39 A dispersion was obtained by carrying out the same operation as in Example 36 except that the amount of the TEOS ethanol preparation solution was 0.34 g. This dispersion was stable and did not cause precipitation, and the electrical conductivity of the conductive film obtained from this dispersion was 6 S / cm. The weight ratio of the other components to the conductive polymer component calculated from the charged ratio was 9.1.
- Example 40 A dispersion was obtained by carrying out the same operation as in Example 36 except that the amount of the TEOS ethanol preparation liquid was changed to 0.46 g. This dispersion was stable and did not precipitate, and the electrical conductivity of the conductive film obtained from this dispersion was 0.2 S / cm. The weight ratio of the other components to the conductive polymer component calculated from the charged ratio was 11.2.
- Example 41 The same operation as in Example 35 was performed to obtain an aqueous dispersion of a composite of poly (3,4-ethylenedioxythiophene) and polyvinyl sulfonic acid.
- This aqueous dispersion was diluted with ion-exchanged water to prepare a solid content of 0.86% by weight (Dispersion B).
- the dispersion B was stable and did not precipitate, and the electrical conductivity of the conductive film obtained from the dispersion B was 13 S / cm.
- the weight ratio of the other components to the conductive polymer component calculated from the charged ratio was 3.0.
- Example 42 0.075 g of a mixed liquid of 1.0866 g of diisopropylamine (manufactured by Kanto Chemical Industry Co., Ltd.) and 10.4512 g of ion-exchanged water is placed in a 20 mL glass container, and then 10.10441 g of the dispersion B obtained in Example 41 is added. The mixture was stirred at room temperature for 2 hours to obtain a dispersion. This dispersion was stable and did not cause precipitation, and the electrical conductivity of the conductive film obtained from this dispersion was 11 S / cm. The weight ratio of the other components to the conductive polymer component calculated from the charged ratio was 3.3.
- Example 43 0.1657 g of a mixed solution of dioctylamine (manufactured by Wako Pure Chemical Industries, Ltd.) 1.0091 g and ion-exchanged water 10.3645 g in a 20 mL glass container, and then the dispersion B 10.010 g obtained in Example 41 was used. In addition, the mixture was stirred at room temperature for 2 hours to obtain a dispersion. This dispersion was stable and did not cause precipitation, and the electrical conductivity of the conductive film obtained from this dispersion was 10 S / cm. The weight ratio of the other components to the conductive polymer component calculated from the charged ratio was 3.7.
- Example 44 0.4971 g of a mixed solution of 1.0091 g of dioctylamine (manufactured by Wako Pure Chemical Industries, Ltd.) and 10.3645 g of ion-exchanged water is placed in a 20 mL glass container, and then 10.0657 g of the dispersion B obtained in Example 41 is used. In addition, the mixture was stirred at room temperature for 2 hours to obtain a dispersion. This dispersion was stable and did not cause precipitation, and the electrical conductivity of the conductive film obtained from this dispersion was 3 S / cm. The weight ratio of the other components to the conductive polymer component calculated from the charged ratio was 5.0.
- Example 45 A mixture of 0.5122 g of hexamethylene diamine (manufactured by Kanto Chemical Co., Ltd.) and 5.4889 g of ion-exchanged water was weighed into a 0.0 mL amount in a 20 mL glass container, and then 10.0721 g of the dispersion B obtained in Example 41 was used. In addition, the mixture was stirred at room temperature for 2 hours to obtain a dispersion. This dispersion was stable and did not cause precipitation, and the electrical conductivity of the conductive film obtained from this dispersion was 13 S / cm. The weight ratio of the other components to the conductive polymer component calculated from the charged ratio was 3.4.
- Example 46 0.7933 g of a mixed solution of butylamine (manufactured by Tokyo Chemical Industry Co., Ltd.) 0.1075 g and ion-exchanged water 9.6078 g is weighed in a 20 mL glass container, and then 200.0871 g of the dispersion B obtained in Example 41 is added. The mixture was stirred at room temperature for 2 hours to obtain a dispersion. This dispersion was stable and did not cause precipitation, and the electrical conductivity of the conductive film obtained from this dispersion was 12 S / cm. The weight ratio of the other components to the conductive polymer component calculated from the charged ratio was 3.2.
- Example 47 0.9649 g of a mixed liquid of amylamine (manufactured by Tokyo Chemical Industry Co., Ltd.) 0.1100 g and ion-exchanged water 9.9165 g was weighed in a 20 mL glass container, and then 20.0474 g of the dispersion B obtained in Example 41 was added. The mixture was stirred at room temperature for 2 hours to obtain a dispersion. This dispersion was stable and did not cause precipitation, and the electrical conductivity of the conductive film obtained from this dispersion was 13 S / cm. The weight ratio of the other components to the conductive polymer component calculated from the charged ratio was 3.2.
- Example 48 A mixed liquid of 0.0167 g of heptylamine (manufactured by Tokyo Chemical Industry Co., Ltd.) and 6.2300 g of ion-exchanged water is weighed into a 20 mL glass container, and 5.2929 g is weighed, and then 20.5180 g of the dispersion B obtained in Example 41 is added. The mixture was stirred at room temperature for 2 hours to obtain a dispersion. This dispersion was stable and did not cause precipitation, and the electrical conductivity of the conductive film obtained from this dispersion was 6 S / cm. The weight ratio of the other components to the conductive polymer component calculated from the charged ratio was 3.3.
- the polyvinyl sulfonic acid of the present invention can be suitably used as a polymer dopant that forms a dispersion having high dispersion stability.
- the dispersion liquid containing the composite of the polyvinyl sulfonic acid and the conductive polymer of the present invention has high dispersion stability, and can form a conductive film having high conductivity without adding a high boiling point organic solvent.
- Such conductive films can be used for various optoelectronic component applications. Examples of the application include applications that require particularly good conductivity, capacitors, conductive films, or conductive sheets.
- the conductive film can be used for applications such as polymer light emitting diodes, organic photovoltaic power generation, secondary batteries, conductive polymer sensors, thin film transistor elements, electroluminescence elements, electrolytic capacitors, and the like. It can also be used as an alternative to the ITO thin film.
Abstract
Description
下記一般式(1)で表されるビニルスルホン酸類ユニットを含むポリビニルスルホン酸であって、
ビニルスルホン酸類モノマー由来のスルホン酸基のモル量が全モノマーユニットのモル量に対して50.0~98.0mol%であり、波長255~800nmの範囲で0.1以上の吸光度(水溶液0.2質量%、セル長10mm)を有するポリビニルスルホン酸。
[2]
重量平均分子量が10,000~800,000である[1]に記載のポリビニルスルホン酸。
[3]
分子量が5,000以下の成分の含有率が10%以下である[1]又は[2]に記載のポリビニルスルホン酸。
[4]
波長475~575nmの範囲で0.1以上の吸光度(水溶液0.2質量%、セル長10mm)を有する[1]~[3]のいずれかに記載のポリビニルスルホン酸。
[5]
下記一般式(1)’で表されるビニルスルホン酸類モノマーを重合してポリビニルスルホン酸を得る工程、及び
前記ポリビニルスルホン酸を、60℃を超える温度で加熱する工程
を含む[1]~[4]のいずれかに記載のポリビニルスルホン酸の製造方法。
[6]
前記加熱する工程において、加熱温度が90~120℃であり、加熱時間が0.5~500時間の範囲である[5]に記載のポリビニルスルホン酸の製造方法。
[7]
前記加熱する工程において、前記ポリビニルスルホン酸が溶媒類と混合した混合物の状態である[5]又は[6]に記載のポリビニルスルホン酸の製造方法。
[8]
[1]~[4]のいずれかに記載のポリビニルスルホン酸と導電性高分子とを含む複合体。
[9]
[8]に記載の複合体を溶媒中に分散させてなる分散液。
[10]
[1]~[4]のいずれかに記載のポリビニルスルホン酸を溶媒中に溶解及び/又は分散させ、該溶解及び/又は分散している溶媒中で、導電性高分子のモノマー類を重合させる工程を含む[9]に記載の分散液の製造方法。
[11]
前記重合させる工程で得られた重合生成物を固体で取り出し当該固体を洗浄する工程、並びに
前記洗浄する工程後の固体を溶媒中に溶解及び/又は分散させる工程
を更に含む[10]に記載の分散液の製造方法。
[12]
[9]に記載の分散液を用いて製造された導電膜。
[13]
[12]に記載の導電膜を含むコンデンサー。
[14]
[12]に記載の導電膜を含む導電性フィルム又は導電性シート。
[15]
ポリ(3,4―エチレンジオキシチオフェン)を含み、
反射法XDR測定において2θが8°~10°の範囲のピークKと2θが24°~28°の範囲のピークLとのピーク面積比(ピークKの面積/ピークLの面積)が1.0~10.0である導電膜。
[16]
導電膜を形成する分散液であって、
前記導電膜が、ポリ(3,4―エチレンジオキシチオフェン)を含み、
前記導電膜の反射法XDR測定において2θが8°~10°の範囲のピークKと2θが24°~28°の範囲のピークLとのピーク面積比(ピークKの面積/ピークLの面積)が1.0~10.0である、分散液。
[17]
導電性高分子及びポリアニオンを含む[16]に記載の分散液。
[18]
前記導電性高分子がポリ(3,4―エチレンジオキシチオフェン)である[17]に記載の分散液。
[19]
前記ポリアニオンが[1]~[4]のいずれかに記載のポリビニルスルホン酸である[17]に記載の分散液。
[20]
[16]~[19]のいずれかに記載の分散液から形成される導電膜。
[21]
ポリアニオンを溶媒中に溶解及び/又は分散させ、該溶解及び/又は分散している溶媒中で、導電性高分子のモノマー類を重合させる工程を含む[16]~[19]のいずれかに記載の分散液の製造方法。
[22]
前記重合させる工程で得られた重合生成物を固体で取り出し当該固体を洗浄する工程、並びに
前記洗浄する工程後の固体を溶媒中に溶解及び/又は分散させる工程
を更に含む[21]に記載の分散液の製造方法。
[23]
[15]又は[20]に記載の導電膜を含むコンデンサー。
[24]
[15]又は[20]に記載の導電膜を含む導電性フィルム又は導電性シート。
本実施の形態のポリビニルスルホン酸は、下記一般式(1)で表されるビニルスルホン酸類ユニットを含むポリビニルスルホン酸であって、
ビニルスルホン酸類モノマー由来のスルホン酸基のモル量が全モノマーユニットのモル量に対して50.0~98.0mol%であり、波長255~800nmの範囲で0.1以上の吸光度(水溶液0.2質量%、セル長10mm)を有する。
本実施の形態のポリビニルスルホン酸は、導電性高分子用の高分子ドーパントとして有用である。本実施の形態のポリビニルスルホン酸がドーパントとして作用する導電性高分子とは、高分子構造内に二重結合と単結合が交互に長く連なった構造を有する高分子をいう。導電性高分子としては、特に限定されないが、例えば、ポリ(p-フェニレン)、ポリ(o-フェニレン)、ポリ(m-フェニレン)、ポリ(2,6-ナフタレン)、ポリ(9,10-アントラセン)等に代表されるポリアリール類;ポリピロール、ポリチオフェン、ポリフラン、ポリセレフェン、ポリピリジン、ポリピリダジン、ポリ(2,2‘-ビピリジン)、ポリピリミジン等に代表されるヘテロアロマティック類;ポリ(p-フェニレンビニレン)、ポリ(1,4-ナフタレンビニレン等に代表されるポリアリールビニレン類;ポリアニリン類;ポリアセチレン類である。上記高分子にいかなる官能基が結合しても構わない。また、導電性高分子は、共重合物であっても構わない。導電性高分子としては、本実施の形態の特異なポリビニルスルホン酸を溶解又は分散した水中での重合性の観点からは、ヘテロアロマティック類が好ましく、ポリピロール、ポリチオフェンがより好ましい。特に好ましいポリチオフェンは、
式(I):
で示される構造単位を有している。
本実施の形態のポリビニルスルホン酸を形成するビニルスルホン酸類モノマーとは、下記一般式(1)’で表される
ビニル基に直接スルホン酸が結合している化合物である。このようなビニルスルホン酸類モノマーとしては、特に限定されないが、例えば、1-アルキルビニルスルホン酸、2-アルキルビニルスルホン酸、1,2-アルキルスルホン酸等のアルキル置換ビニルスルホン酸;ビニルスルホン酸ナトリウム、1-アルキルビニルスルホン酸ナトリウム、ビニルスルホン酸カリウム、ビニルスルホン酸アンモニウム、ビニルスルホン酸アルキルアミン塩等のスルホン酸塩;ビニルスルホン酸フルオライド、ビニルスルホン酸クロライド等のスルホン酸ハロゲン化物;ビニルスルホン酸等が代表的なビニルスルホン酸類モノマーとして挙げられる。これらの中で、R1、R2、R3が水素でZが水素又はナトリウム、カリウムであるビニルスルホン酸及びビニルスルホン酸塩が好ましいモノマーと挙げられる。
本実施の形態において、「ポリマー中の全てのモノマーユニットのモル量」とは、ポリマー構成モノマーを、多重結合を有するモノマーとし、該ポリマーを重合する為の該モノマーのモル量が最大となるモノマーにより該ポリマーが構成されているとした場合の該ポリマー構成モノマーのモル量である。
本実施の形態のポリビニルスルホン酸において、ポリマー中のビニルスルホン酸類モノマー由来のスルホン酸基が導電性高分子のドーピング剤として好適に使用される。このスルホン酸基は、高分子主鎖とスルホン酸基との間にフェニル基等を有しない。そのため、本実施の形態のポリビニルスルホン酸は、ポリマー重量に対するスルホン酸基重量が非常に高くなり、高分子ドーパント重量に対するドーピング量が非常に高い優れたドーピング剤である。従来、該スルホン酸基は、高分子主鎖の運動により容易に運動してしまい導電性高分子へのドーピングの状態が不安定となるという問題を抱えているが、本実施の形態においては、該スルホン酸基の運動が高分子主鎖の運動による影響を少なくするスルホン酸基量を発見し、該ポリビニルスルホン酸より、高く安定した導電性高分子-ドーパント複合体を製造することができる。すなわち、本実施の形態のポリビニルスルホン酸は、ビニルスルホン酸類モノマー由来のスルホン酸基のモル量をポリマー中の全モノマーユニットのモル量に対して50.0~98.0mol%の範囲にする。ビニルスルホン酸類モノマー由来のスルホン酸基のモル量(mol%)が前記下限値以上の場合は、ポリマー重量当たりのドーピング量が向上するので、好ましく、該スルホン酸基のモル量(mol%)が前記上限値以下の場合は、該スルホン酸基が高分子主鎖の運動の影響を受け難くなり、安定した導電性高分子-ドーパント複合体が形成できる。好ましい該スルホン酸基のモル量は85.0~97.0mol%である。該スルホン酸基のモル量は、後述のポリビニルスルホン酸を加熱処理すること、あるいは架橋剤を配合することなどによって達成することができる。なお、本実施の形態において、スルホン酸基とは2分子のスルホン酸が脱水縮合した無水物を含む。加熱処理を実施し、脱スルホンと同時にスルホン酸基2分子で脱水縮合した無水物を含むポリビニルスルホン酸は好ましいポリマーである。
本実施の形態の、ビニルスルホン酸類モノマー由来のスルホン酸基のモル量が上記特定の範囲にあり、波長255~800nmの範囲で上記特定の吸光度を有するポリビニルスルホン酸の製造方法は、好適には下記に示す、より少ない工程で製造する方法によって得ることができる。
ビニルスルホン酸類モノマーを用い重合を行い、ポリビニルスルホン酸を製造することができる。
本実施の形態の複合体は、上述のポリビニルスルホン酸と導電性高分子とを含む。
本実施の形態の分散液は、上述の複合体を溶媒中に分散させてなる。
本実施の形態の分散液の製造方法は、特に限定されないが、通常、ポリアニオン(例えば、上述のポリビニルスルホン酸)を溶媒中に溶解及び/又は分散させ、該溶解及び/又は分散している溶媒中で、導電性高分子のモノマー類を重合させる工程を含む。
で表される3,4-ジオキシチオフェンを単独重合又は共重合することによって製造される。
本実施の形態の導電膜は、上述の分散液を用いて製造された導電膜である。例えば、上述の分散液を、基材上に塗布して成膜し、導電膜とすることができる。
式(I):
で示される構造単位を有している。
<ゲルパーミエーションクロマトグラフ(GPC)測定>
各ポリマーの重量平均分子量を知るための標準溶液として、東ソー株式会社製の分子量900000、250000、107000、50000、21000、4100の各標準ポリエチレンオキサイドについて1000ppmの水溶液を作成し用いた。
島津製作所製UV-2450を用い、255nm、475nm、525nm、575nm、800nmの各波長における吸光度を測定した。具体的には、測定試料を0.2重量%の濃度でイオン交換水に溶解させ、得られた水溶液を光路長10mmの石英セルに入れ、前記条件でUV測定を行った。
固形分として約0.1gを測定試料とした。該測定試料をイオン交換水50mlに充分溶解させた後、得られた溶液について、京都電子工業株式会社製、電位差自動滴定装置AT-610を用い、シグマアルドリッチ社製0.1mol/L水酸化ナトリウムを滴定液として、電位差滴定を行った。滴定の終点は、得られる滴定曲線の変曲点とした。該変曲点における滴定液の滴定量を読み取り、次の数式(1)に当てはめることにより、ポリマー試料中のスルホン酸基のモル量(mol%)を算出した。
実施例及び比較例で得られた水分散体を76×26mmのスライドガラス上にドロップし120℃で30分間乾燥させ導電膜を作成した。
前記作成した導電膜の表面抵抗率を、株式会社三菱化学アナリテック製ロレスターGP(MCP-T610)を用い、4探針法により測定した。また、前記作成した導電膜の膜厚を、株式会社ミツトヨ製、デジマチックインジケータID-C112CXを用い測定した。該測定後、次の数式(2)により、導電膜の電気伝導度を算出した。
実施例及び比較例で得られた水分散体の安定性について以下の基準により評価した。
○:水分散体中に沈殿が生じなかった。
×:水分散体中に沈殿が生じた。
各導電膜のXRD測定は、リガク社製Ultima-IVを用い、X線波長0.154nmとし、走査範囲を2θ=5~60deg(0.02deg刻み)、走査速度4.0deg/minで行った。得られたXRDプロファイルを定量的に評価するため、次の方法でピーク分離を行った。
2θ=19°ピークの低角側の裾と2θ=26°ピークの広角側の裾とを結ぶ直線をバックグラウンドとして反射法XRDプロフィールから引き去った。次に、ピークが観測された5°<2θ<30°において、2θ=3°、9°、19°、23°、26°をピーク位置の初期値とする5個のガウス分布(下記式5)で、バックグラウンド補正後のXRDプロフィールをピーク分離した。
各分散液における分散質の平均粒子径は大塚電子製FPAR-1000を用いて下記条件で測定を行った。
測定試料:分散液を50倍にイオン交換水で希釈したもの。
測定プローブ:希薄系プローブ。
粒径解析:MARQUARDT法。
本実施例中の導電膜の耐熱試験は、以下のとおり行った。まず該分散液を25×25mmのスライドガラス上にスピンコートし、100℃で30分間乾燥させ導電膜を作成した。該導電膜をエスペック株式会社製、小型高温チャンバーに入れ、135℃で55時間加熱した。該加熱前後の導電膜の表面抵抗値を、株式会社三菱化学アナリテック製ロレスターGP(MCP-T610)を用い、4探針法により測定した。該導電膜の加熱による表面抵抗率の増加割合は次式により求めた。
本実施例中のポリビニルスルホン酸の固体NMR測定は日本電子製ECA700を用いて下記条件で行った。
測定核:13C。
測定法:CP/MAS法。
観測周波数:176.05MHz。
分析試料管:4mmφのNMR管。
MAS:10kHz。
積算回数:1000回。
〈ポリビニルスルホン酸の調製〉重量平均分子量Mw9.6×103
パドル型攪拌翼、ジムロート冷却管、温度計及び窒素導入管を備えたガラス製2000mLフラスコにイオン交換水1120gを入れ、ビニルスルホン酸(CH2=CH-SO3H、旭化成ファインケム株式会社製、以下「VSA」ともいう)480gを攪拌冷却しながら混合した。次に、前記フラスコにラジカル重合開始剤2,2’-アゾビス(2-メチルプロピオンアミジン)二塩酸塩(和光純薬工業株式会社製、以下、「V-50」ともいう)を0.480g仕込み、窒素バブリングを30分続け窒素置換を行った。その後、前記フラスコ内の水溶液を、60℃で11時間攪拌し、ラジカル重合開始剤V-50を0.486g加え、60℃で6時間攪拌した。更にラジカル重合開始剤V-50を0.482g加えた後、70℃に昇温し10時間攪拌を行ってポリビニルスルホン酸(PVS)水溶液を得た。得られたポリビニルスルホン酸(PVS)をGPCで測定したところ、重量平均分子量は9.6×103であり、残存VSAは0.4%であった。
〈ポリビニルスルホン酸の調製〉重量平均分子量Mw 3.3×104
アンカー型攪拌翼、ジムロート冷却管、温度計及び窒素導入管を備えたガラス製2000mLセパラブルフラスコにイオン交換水736gを入れ、VSA864gを攪拌冷却しながら混合した。次に、前記フラスコにラジカル重合開始剤V-50を0.864g仕込み、窒素バブリングを30分続け窒素置換を行った。その後、前記フラスコ内の水溶液を、40℃で11時間攪拌し、ラジカル重合開始剤V-50を0.864g加え、更に40℃で13時間攪拌した。その後70℃に昇温し10時間攪拌を続けてポリビニルスルホン酸(PVS)水溶液を得た。得られたポリビニルスルホン酸(PVS)をGPCで測定したところ、重量平均分子量は3.3×104であり、残存VSAは0.2%であった。
〈ポリビニルスルホン酸の調製〉重量平均分子量Mw 5.3×104
製造例2と同様のフラスコにイオン交換水420gを入れ、VSA980gを攪拌冷却しながら混合した。次に、前記フラスコにラジカル重合開始剤V-50を0.196g仕込み、窒素バブリングを30分続け窒素置換を行った。その後、前記フラスコ内の水溶液を、40℃で24時間攪拌し、ラジカル重合開始剤V-50を0.98g加え、50℃に昇温した後48時間攪拌を続けてポリビニルスルホン酸(PVS)水溶液を得た。得られたポリビニルスルホン酸(PVS)をGPCで測定したところ、重量平均分子量は5.3×104であり、残存VSAは0.1%であった。
〈ポリビニルスルホン酸の調製〉重量平均分子量Mw 2×105
パドル型攪拌翼、温度計及び窒素導入管を備えたガラス製500mLフラスコにイオン交換水25gを入れ、VSA225gを攪拌冷却しながら混合した。次に前記フラスコにラジカル重合開始剤2,2’-アゾビス[2-(2-イミダゾリン-2-イル)プロパン]二塩酸塩)(和光純薬工業株式会社製)を1.125g仕込み、窒素バブリングを30分続け窒素置換を行った。その後、前記フラスコ内の水溶液を、10℃で27時間攪拌して重合液を得た。得られた重合液について、テトラヒドロフランを再沈溶媒として用い、残存VSAが1%以下になるまで再沈殿精製を繰り返してポリビニルスルホン酸(PVS)水溶液を得た。得られたポリビニルスルホン酸(PVS)をGPCで測定したところ、重量平均分子量は2.0×105であり、残存VSAは0.5%であった。
〈ポリビニルスルホン酸の調製〉K塩経由 重量平均分子量Mw 3.2×104
パドル型攪拌翼、温度計及び窒素導入管を備えたガラス製100mLフラスコにイオン交換水24.16gを入れ、VSA43.11gを冷却攪拌し混合した。次に、前記フラスコに50重量%の水酸化カリウム水溶液を冷却しながら攪拌下で加えた。次いで、前記フラスコにラジカル重合開始剤V-50を0.066g加え、窒素バブリングを30分続け窒素置換を行った。その後、前記フラスコ内の水溶液を、40℃で40時間攪拌し重合を行って重合液を得た。得られた重合液をイオン交換水917.74gと混合し、5.7重量%のポリビニルスルホン酸カリウム水溶液を調製した。あらかじめ塩酸で再生した強酸性イオン交換樹脂(DOWEX(登録商標)モノスフィア 650C)400mLを充填したカラム塔(内径50mm、高さ600mm)に、前記調製したポリビニルスルホン酸カリウム水溶液を毎時200mLの速度で流入し、次にイオン交換水680gで洗浄して脱カリウム処理を行った。その後、脱カリウム処理を行った水溶液を、エバポレータを用い40℃で減圧濃縮して、67.69gのポリビニルスルホン酸(PVS)水溶液を得た。得られたポリビニルスルホン酸(PVS)をGPCで測定したところ、重量平均分子量は3.2×104であり、残存VSAは0.6%であった。
〈ポリビニルスルホン酸の調製〉Na塩経由 重量平均分子量Mw 2.9×104
パドル型攪拌翼、温度計及び窒素導入管を備えたガラス製100mLフラスコにイオン交換水26.40gを入れ、VSA34.40gを冷却攪拌し混合した。次に、前記フラスコに48重量%の水酸化ナトリウム水溶液を27.10g、冷却しながら攪拌下で加えた。その後、前記フラスコにラジカル重合開始剤V-50を0.052g加え、窒素バブリングを30分続け窒素置換を行った。その後、前記フラスコ内の水溶液を、40℃で45時間攪拌し重合を行って重合液を得た。得られた重合液をイオン交換水522gと混合し、5.6重量%のポリビニルスルホン酸ナトリウム水溶液を調製した。あらかじめ塩酸で再生した強酸性イオン交換樹脂(DOWEX(登録商標)モノスフィア 650C)350mLを充填したカラム塔(内径50mm、高さ600mm)に、ポリビニルスルホン酸ナトリウム水溶液を毎時150mLの速度で流入し、次にイオン交換水540gで洗浄して脱ナトリウム処理を行った。その後、脱ナトリウム処理を行った水溶液を、エバポレータを用い40℃で減圧濃縮して、60.4gのポリビニルスルホン酸(PVS)水溶液を得た。得られたポリビニルスルホン酸(PVS)をGPCで測定したところ、重量平均分子量は2.9×104であり、残存VSAは0.7%であった。
製造例1で得られたPVS水溶液を50℃で72時間加熱真空乾燥し、PVS固体を得た。得られたPVS固体の水分は13.5重量%であった。このPVS固体を100mLビーカーに2g仕込み、送風乾燥機による加熱処理を110℃で10時間行った。当該加熱処理したPVSについて上記のとおりGPC測定、吸光度測定及びスルホン酸基のモル量の測定を行った。結果を表1に示す。
製造例2で得られたPVS水溶液を用い、PVS固体を得た後の加熱処理時間を1時間としたこと以外は実施例1と同様の操作を実施し、加熱処理したPVS、ポリ(3,4-エチレンジオキシチオフェン)とポリビニルスルホン酸との複合体の水分散体、導電膜を得た。
PVS固体を得た後の加熱処理時間を5時間としたこと以外は実施例2と同様の操作を実施し、加熱処理したPVS、ポリ(3,4-エチレンジオキシチオフェン)とポリビニルスルホン酸との複合体の水分散体、導電膜を得た。
PVS固体を得た後の加熱処理時間を7.5時間としたこと以外は実施例2と同様の操作を実施し、加熱処理したPVS、ポリ(3,4-エチレンジオキシチオフェン)とポリビニルスルホン酸との複合体の水分散体、導電膜を得た。
PVS固体を得た後の加熱処理時間を10時間としたこと以外は実施例2と同様の操作を実施し、加熱処理したPVS、ポリ(3,4-エチレンジオキシチオフェン)とポリビニルスルホン酸との複合体の水分散体、導電膜を得た。
PVS固体を得た後の加熱処理時間を12.5時間としたこと以外は実施例2と同様の操作を実施し、加熱処理したPVS、ポリ(3,4-エチレンジオキシチオフェン)とポリビニルスルホン酸との複合体の水分散体、導電膜を得た。
PVS固体を得た後の加熱処理時間を15時間としたこと以外は実施例2と同様の操作を実施し、加熱処理したPVS、ポリ(3,4-エチレンジオキシチオフェン)とポリビニルスルホン酸との複合体の水分散体、導電膜を得た。
PVS固体を得た後の加熱処理温度を100℃とし、加熱処理時間を48時間としたこと以外は実施例2と同様の操作を実施し、加熱処理したPVS、ポリ(3,4-エチレンジオキシチオフェン)とポリビニルスルホン酸との複合体の水分散体、導電膜を得た。
PVS固体を得た後の加熱処理温度を100℃とし、加熱処理時間を72時間としたこと以外は実施例2と同様の操作を実施し、加熱処理したPVS、ポリ(3,4-エチレンジオキシチオフェン)とポリビニルスルホン酸との複合体の水分散体、導電膜を得た。
PVS固体を得た後の加熱処理温度を95℃とし、加熱処理時間を24時間としたこと以外は実施例2と同様の操作を実施し、加熱処理したPVS、ポリ(3,4-エチレンジオキシチオフェン)とポリビニルスルホン酸との複合体の水分散体、導電膜を得た。
PVS固体を得た後の加熱処理温度を95℃とし、加熱処理時間を72時間としたこと以外は実施例2と同様の操作を実施し、加熱処理したPVS、ポリ(3,4-エチレンジオキシチオフェン)とポリビニルスルホン酸との複合体の水分散体、導電膜を得た。
PVS固体を得た後の加熱処理温度を95℃とし、加熱処理時間を96時間としたこと以外は実施例2と同様の操作を実施し、加熱処理したPVS、ポリ(3,4-エチレンジオキシチオフェン)とポリビニルスルホン酸との複合体の水分散体、導電膜を得た。
PVS固体を得た後の加熱処理温度を95℃とし、加熱処理時間を120時間としたこと以外は実施例2と同様の操作を実施し、加熱処理したPVS、ポリ(3,4-エチレンジオキシチオフェン)とポリビニルスルホン酸との複合体の水分散体、導電膜を得た。
PVS固体を得た後の加熱処理温度を95℃とし、加熱処理時間を144時間としたこと以外は実施例2と同様の操作を実施し、加熱処理したPVS、ポリ(3,4-エチレンジオキシチオフェン)とポリビニルスルホン酸との複合体の水分散体、導電膜を得た。
PVS固体を得た後の加熱処理温度を95℃とし、加熱処理時間を192時間としたこと以外は実施例2と同様の操作を実施し、加熱処理したPVS、ポリ(3,4-エチレンジオキシチオフェン)とポリビニルスルホン酸との複合体の水分散体、導電膜を得た。
PVS固体を得た後の加熱処理温度を95℃とし、加熱処理時間を240時間としたこと以外は実施例2と同様の操作を実施し、加熱処理したPVS、ポリ(3,4-エチレンジオキシチオフェン)とポリビニルスルホン酸との複合体の水分散体、導電膜を得た。
製造例3で得られたPVS水溶液を用い、PVS固体を得た後の加熱処理温度を115℃とし、加熱処理時間を1時間としたこと以外は実施例1と同様の操作を実施し、加熱処理したPVS、ポリ(3,4-エチレンジオキシチオフェン)とポリビニルスルホン酸との複合体の水分散体、導電膜を得た。
PVS固体を得た後の加熱処理時間を2時間としたこと以外は実施例17と同様の操作を実施し、加熱処理したPVS、ポリ(3,4-エチレンジオキシチオフェン)とポリビニルスルホン酸との複合体の水分散体、導電膜を得た。
PVS固体を得た後の加熱処理時間を4時間としたこと以外は実施例17と同様の操作を実施し、加熱処理したPVS、ポリ(3,4-エチレンジオキシチオフェン)とポリビニルスルホン酸との複合体の水分散体、導電膜を得た。
PVS固体を得た後の加熱処理温度を110℃とし、加熱処理時間を3時間としたこと以外は実施例17と同様の操作を実施し、加熱処理したPVS、ポリ(3,4-エチレンジオキシチオフェン)とポリビニルスルホン酸との複合体の水分散体、導電膜を得た。
PVS固体を得た後の加熱処理温度を110℃とし、加熱処理時間を4時間としたこと以外は実施例17と同様の操作を実施し、加熱処理したPVS、ポリ(3,4-エチレンジオキシチオフェン)とポリビニルスルホン酸との複合体の水分散体を得た。
PVS固体を得た後の加熱処理温度を110℃とし、加熱処理時間を5時間としたこと以外は実施例17と同様の操作を実施し、加熱処理したPVS、ポリ(3,4-エチレンジオキシチオフェン)とポリビニルスルホン酸との複合体の水分散体、導電膜を得た。
PVS固体を得た後の加熱処理温度を110℃とし、加熱処理時間を7.5時間としたこと以外は実施例17と同様の操作を実施し、加熱処理したPVS、ポリ(3,4-エチレンジオキシチオフェン)とポリビニルスルホン酸との複合体の水分散体、導電膜を得た。
PVS固体を得た後の加熱処理温度を110℃とし、加熱処理時間を10時間としたこと以外は実施例17と同様の操作を実施し、加熱処理したPVS、ポリ(3,4-エチレンジオキシチオフェン)とポリビニルスルホン酸との複合体の水分散体、導電膜を得た。
PVS固体を得た後の加熱処理温度を100℃とし、加熱処理時間を72時間としたこと以外は実施例17と同様の操作を実施し、加熱処理したPVS、ポリ(3,4-エチレンジオキシチオフェン)とポリビニルスルホン酸との複合体の水分散体、導電膜を得た。
PVS固体を得た後の加熱処理を行わなかったこと以外は実施例1と同様の操作を実施した。得られた水分散体は沈殿物が発生していた。
PVS固体を得た後の加熱処理を行わなかったこと以外は実施例2と同様の操作を実施した。得られた水分散体は沈殿物が発生していた。
PVS固体を得た後の加熱処理を行わなかったこと以外は実施例17と同様の操作を実施した。得られた水分散体は沈殿物が発生していた。
製造例4で得られたPVS水溶液を用い、PVS固体を得た後の加熱処理を行わなかったこと以外は実施例1と同様の操作を実施した。得られた水分散体は少量の沈殿物が発生していた。
加熱処理したPVSの使用量を0.4gにしたこと以外は実施例10と同様の操作を実施し、ポリ(3,4-エチレンジオキシチオフェン)とポリビニルスルホン酸との複合体の水分散体を得た。この水分散体は安定で沈殿が生じることはなかった。また、この水分散体から得られた導電膜の電気伝導度は5S/cmであった。仕込み割合から計算された導電性高分子成分に対するそれ以外の成分の重量比は2.0であった。
加熱処理したPVSの使用量を0.8gにしたこと以外は実施例10と同様の操作を実施し、ポリ(3,4-エチレンジオキシチオフェン)とポリビニルスルホン酸との複合体の水分散体を得た。この水分散体は安定で沈殿が生じることはなかった。また、この水分散体から得られた導電膜の電気伝導度は20S/cmであった。仕込み割合から計算された導電性高分子成分に対するそれ以外の成分の重量比は4.0であった。
加熱処理したPVSの使用量を0.4gにしたこと以外は実施例11と同様の操作を実施し、ポリ(3,4-エチレンジオキシチオフェン)とポリビニルスルホン酸との複合体の水分散体を得た。この水分散体は安定で沈殿が生じることはなかった。また、この水分散体から得られた導電膜の電気伝導度は23S/cmであった。仕込み割合から計算された導電性高分子成分に対するそれ以外の成分の重量比は2.0であった。
加熱処理したPVSの使用量を0.8gにしたこと以外は実施例11と同様の操作を実施し、ポリ(3,4-エチレンジオキシチオフェン)とポリビニルスルホン酸との複合体の水分散体を得た。この水分散体は安定で沈殿が生じることはなかった。また、この水分散体から得られた導電膜の電気伝導度は29S/cmであった。仕込み割合から計算された導電性高分子成分に対するそれ以外の成分の重量比は4.0であった。
加熱処理したPVSの使用量を0.4gにしたこと以外は実施例13と同様の操作を実施し、ポリ(3,4-エチレンジオキシチオフェン)とポリビニルスルホン酸との複合体の水分散体を得た。この水分散体は安定で沈殿が生じることはなかった。また、この水分散体から得られた導電膜の電気伝導度は33S/cmであった。仕込み割合から計算された導電性高分子成分に対するそれ以外の成分の重量比は2.0であった。
加熱処理したPVSの使用量を0.8gにしたこと以外は実施例13と同様の操作を実施し、ポリ(3,4-エチレンジオキシチオフェン)とポリビニルスルホン酸との複合体の水分散体を得た。この水分散体は安定で沈殿が生じることはなかった。また、この水分散体から得られた導電膜の電気伝導度は16S/cmであった。仕込み割合から計算された導電性高分子成分に対するそれ以外の成分の重量比は4.0であった。
加熱処理したPVSの使用量を0.2gにしたこと以外は実施例14と同様の操作を実施し、ポリ(3,4-エチレンジオキシチオフェン)とポリビニルスルホン酸との複合体の水分散体を得た。この水分散体は安定で沈殿が生じることはなかった。この水分散体から得られた導電膜の電気伝導度は22S/cmであった。仕込み割合から計算された導電性高分子成分に対するそれ以外の成分の重量比は1.0であった。
60mLガラス容器に、ポリスチレンスルホン酸(PSS)水溶液(シグマアルドリッチ社製、固形分18重量%)を1.11g、イオン交換水38.19g、及び過硫酸ナトリウム(シグマアルドリッチ社製)0.5gを仕込み攪拌混合した。次いでEDOT0.2gを加え、室温で24時間攪拌混合し、酸化重合を行った。その後、この反応混合物に陽イオン交換樹脂7.5g及び陰イオン交換樹脂7.5gを加え、20時間攪拌混合し、ろ別して脱塩されたポリ(3,4-エチレンジオキシチオフェン)とポリスチレンスルホン酸との複合体の水分散体を得た。この水分散体から得られた導電膜の電気伝導度は2.7S/cmであった。仕込み割合から計算された導電性高分子成分に対するそれ以外の成分の重量比は1.0であった。
PSS水溶液の配合量を2.22gとし、イオン交換水の配合量を37.08gとしたこと以外は比較例5と同様の操作を実施し、ポリ(3,4-エチレンジオキシチオフェン)とポリスチレンスルホン酸との複合体の水分散体を得た。この水分散体から得られた導電膜の電気伝導度は3.2S/cmであった。仕込み割合から計算された導電性高分子成分に対するそれ以外の成分の重量比は2.0であった。
PSS水溶液の配合量を3.33gとし、イオン交換水の配合量を35.97gとしたこと以外は比較例5と同様の操作を実施し、ポリ(3,4-エチレンジオキシチオフェン)とポリスチレンスルホン酸との複合体の水分散体を得た。この水分散体から得られた導電膜の電気伝導度は4.3S/cmであった。仕込み割合から計算される導電性高分子成分に対するそれ以外の成分の重量比は3.0であった。
PSS水溶液の配合量を4.44g、イオン交換水の配合量を34.86gとしたこと以外は比較例5と同様の操作を実施し、ポリ(3,4-エチレンジオキシチオフェン)とポリスチレンスルホン酸との複合体の水分散体を得た。この水分散体から得られた導電膜の電気伝導度は3.2S/cmであった。仕込み割合から計算される導電性高分子成分に対するそれ以外の成分の重量比は4.0であった。
製造例2で得られたPVS水溶液を用い、PVS固体を得た後の加熱処理温度を130℃とし加熱処理時間を1時間としたこと以外は実施例1と同様の操作を実施し、加熱処理したPVS、ポリ(3,4-エチレンジオキシチオフェン)とポリビニルスルホン酸との複合体の水分散体、導電膜を得た。加熱処理したPVS(ドーパント)の各種分析結果、ポリ(3,4-エチレンジオキシチオフェン)とポリビニルスルホン酸との複合体の水分散体の評価結果、ならびに導電膜の電気伝導度及びXRDの測定結果を表1-1に示す。
製造例2で得られたPVS水溶液を用い、PVS固体を得た後の加熱処理温度を150℃とし加熱処理時間を1時間としたこと以外は実施例1と同様の操作を実施し、加熱処理したPVS、ポリ(3,4-エチレンジオキシチオフェン)とポリビニルスルホン酸との複合体の水分散体、導電膜を得た。加熱処理したPVS(ドーパント)の各種分析結果、ポリ(3,4-エチレンジオキシチオフェン)とポリビニルスルホン酸との複合体の水分散体の評価結果、ならびに導電膜の電気伝導度及びXRDの測定結果を表1-1に示す。
製造例3で得られたPVS水溶液を、50℃で72時間加熱真空乾燥し、PVS固体を得た。その後、このPVS固体を100mLビーカーに2g仕込み、送風乾燥機による加熱処理を90℃で480時間行った。当該加熱処理したPVSについて上記のとおりGPC測定、吸光度測定及びスルホン酸基のモル量の測定を行った。結果を表1-1に示す。
製造例2で得られたPVS水溶液を、50℃で72時間加熱真空乾燥し、PVS固体を得た。その後、このPVS固体を2000mLセパラブルフラスコに100g仕込み、トルエン1200gを加えて溶液を得た。得られた溶液を、ディーンスターク、ジムロート、攪拌翼を備えた装置で110℃、8時間加熱した。その後、前記溶液を冷却し、トルエンをデンカントして50℃、2torrで減圧乾燥してPVS固体を得た。残存するトルエンを除去すべく、前記PVS固体を18.0gを1000mLナスフラスコに仕込み、イオン交換水750.0gで溶解し、エバポレータを用いて50℃バス、減圧下でトルエンと水とを、トルエンがなくなるまで共沸留去した。当該加熱処理したPVSについて上記のとおりGPC測定、吸光度測定及びスルホン酸基のモル量の測定を行った。結果を表1-1に示す。
製造例2で得られたPVS水溶液を、50℃で72時間加熱真空乾燥し、PVS固体を得た。その後、このPVS固体を2000mLセパラブルフラスコに100g仕込み、トルエン1200gを加えて溶液を得た。得られた溶液を、ディーンスターク、ジムロート、攪拌翼を備えた装置で110℃、8時間加熱した。その後、前記溶液を冷却し、トルエンをデンカントして50℃、2torrで減圧乾燥してPVS固体を得た。さらに残存するトルエンを除去すべく、前記PVS固体を18.0gを1000mLナスフラスコに仕込み、イオン交換水550.0gで溶解し、エバポレータを用いて50℃バス、減圧下でトルエンと水とを、トルエンがなくなるまで共沸留去した。
アルドリッチ社製PEDOT/PSS分散液(製品名;Poly(3,4-ethylenedioxythiophene)-poly(styrenesulfonate)1.3wt% dispersion in H2O,conductive grade、製品番号;483095)から上記のとおり導電膜を作成し、該導電膜の電気伝導度とXRDとを測定した。評価結果を表1-3に示す。該分散液から得られる導電膜を上記のとおり耐熱試験を行った。加熱前の表面抵抗率は1.0×105Ω/□、加熱後の表面抵抗率は1.9×106Ω/□であり、表面抵抗率の増加割合は17.0であった。
分散液をヘレウス社製PEDOT/PSS分散液(商品名PH500)にしたこと以外は比較例10と同様の評価を行った。評価結果を表1-3に示す。
製造例5で得られたPVS水溶液を用い、PVS固体を得た後の加熱処理時間を5時間としたこと以外は実施例1と同様の操作を実施し、加熱処理したPVS、ポリ(3,4-エチレンジオキシチオフェン)とポリビニルスルホン酸との複合体の水分散体、導電膜を得た。加熱処理したPVSの吸光度は255nmで0.533、525nmで0.264、800nmで0.023であり、スルホン酸基のモル量は96.2mol%であった。この分散液は安定で沈殿が生じることはなく、この分散液から得られた導電膜の電気伝導度は35S/cmであった。
製造例6で得られたPVS水溶液を用いたこと以外は実施例1と同様の操作を実施し、加熱処理したPVS、ポリ(3,4-エチレンジオキシチオフェン)とポリビニルスルホン酸との複合体の水分散体、導電膜を得た。加熱処理したPVSの吸光度は255nmで1.210、525nmで0.612、800nmで0.209であり、スルホン酸基のモル量は89.5mol%であった。この分散液は安定で沈殿が生じることはなく、この分散液から得られた導電膜の電気伝導度は32S/cmであった。
製造例2で得られたPVS水溶液を50℃で72時間加熱真空乾燥し、PVS固体を得た。得られたPVS固体を300mLビーカーに20g仕込み、送風乾燥機による加熱処理を110℃で10時間行った。この加熱処理したPVSの255、525、800nmにおける吸光度はそれぞれ0.988、0.332、0.165であり、スルホン酸基のモル量は86.5mol%であった。攪拌機及び温度計を備えた2000mLガラス製フラスコに加熱処理したPVS15gを入れ、イオン交換水967gで溶解させ、EDOT5g、過硫酸ナトリウム(シグマアルドリッチ社製)12.57gを加え、20℃で24時間攪拌混合し、酸化重合を行った。次いで、この反応混合物に陽イオン交換樹脂100g及び陰イオン交換樹脂100gを加え、20時間攪拌混合し、ろ別して脱塩されたポリ(3,4-エチレンジオキシチオフェン)とポリビニルスルホン酸との複合体の水分散体を得た。
テトラエトキシシラン(東京化成工業株式会社製、以下「TEOS」ともいう)2.05gとエタノール(シグマアルドリッチ社製)2.31gとの混合溶液(混合割合よりTEOSは47重量%、以下「TEOSエタノール調製液」ともいう)を0.08g、20mLガラス容器にはかり採り、実施例35で得られた分散液Aを15g加え、室温で20時間混合攪拌を行って分散液を得た。この分散液は安定で沈殿が生じることはなく、この分散液から得られた導電膜の電気伝導度は12S/cmであった。仕込み割合から計算された導電性高分子成分に対するそれ以外の成分の重量比は4.4であった。
TEOSエタノール調製液の配合量を0.12gとしたこと以外は実施例36と同様の操作を実施して分散液を得た。この分散液は安定で沈殿が生じることはなく、この分散液から得られた導電膜の電気伝導度は13S/cmであった。仕込み割合から計算された導電性高分子成分に対するそれ以外の成分の重量比は5.1であった。
TEOSエタノール調製液の配合量を0.22gとしたこと以外は実施例36と同様の操作を実施して分散液を得た。この分散液は安定で沈殿が生じることはなく、この分散液から得られた導電膜の電気伝導度は11S/cmであった。仕込み割合から計算された導電性高分子成分に対するそれ以外の成分の重量比は6.9であった。
TEOSエタノール調製液の配合量を0.34gとしたこと以外は実施例36と同様の操作を実施して分散液を得た。この分散液は安定で沈殿が生じることはなく、この分散液から得られた導電膜の電気伝導度は6S/cmであった。仕込み割合から計算された導電性高分子成分に対するそれ以外の成分の重量比は9.1であった。
TEOSエタノール調製液の配合量を0.46gとしたこと以外は実施例36と同様の操作を実施して分散液を得た。この分散液は安定で沈殿が生じることはなく、この分散液から得られた導電膜の電気伝導度は0.2S/cmであった。仕込み割合から計算された導電性高分子成分に対するそれ以外の成分の重量比は11.2であった。
実施例35と同様の操作を実施し、ポリ(3,4-エチレンジオキシチオフェン)とポリビニルスルホン酸との複合体の水分散体を得た。
ジイソプロピルアミン(関東化学工業株式会社製)1.0866gとイオン交換水10.4512gとの混合液を20mLガラス容器に0.075gはかり採り、次いで実施例41で得られた分散液B10.1441gを加え、室温で2時間攪拌して分散液を得た。この分散液は安定で沈殿が生じることはなく、この分散液から得られた導電膜の電気伝導度は11S/cmであった。仕込み割合から計算された導電性高分子成分に対するそれ以外の成分の重量比は3.3であった。
ジオクチルアミン(和光純薬工業株式会社製)1.0091gとイオン交換水10.3645gとの混合液を20mLガラス容器に0.1657gはかり採り、次いで実施例41で得られた分散液B10.010gを加え、室温で2時間攪拌して分散液を得た。この分散液は安定で沈殿が生じることはなく、この分散液から得られた導電膜の電気伝導度は10S/cmであった。仕込み割合から計算された導電性高分子成分に対するそれ以外の成分の重量比は3.7であった。
ジオクチルアミン(和光純薬工業株式会社製)1.0091gとイオン交換水10.3645gとの混合液を20mLガラス容器に0.4971gはかり採り、次いで実施例41で得られた分散液B10.0657gを加え、室温で2時間攪拌して分散液を得た。この分散液は安定で沈殿が生じることはなく、この分散液から得られた導電膜の電気伝導度は3S/cmであった。仕込み割合から計算された導電性高分子成分に対するそれ以外の成分の重量比は5.0であった。
ヘキサメチレンジアミン(関東化学工業株式会社製)0.5122gとイオン交換水5.4889gとの混合液を20mLガラス容器に0.0814gはかり採り、次いで実施例41で得られた分散液B10.0721gを加え、室温で2時間攪拌して分散液を得た。この分散液は安定で沈殿が生じることはなく、この分散液から得られた導電膜の電気伝導度は13S/cmであった。仕込み割合から計算された導電性高分子成分に対するそれ以外の成分の重量比は3.4であった。
ブチルアミン(東京化成工業株式会社製)0.1075gとイオン交換水9.6078gとの混合液を20mLガラス容器に0.7933gはかり採り、次いで実施例41で得られた分散液B20.0871gを加え、室温で2時間攪拌して分散液を得た。この分散液は安定で沈殿が生じることはなく、この分散液から得られた導電膜の電気伝導度は12S/cmであった。仕込み割合から計算された導電性高分子成分に対するそれ以外の成分の重量比は3.2であった。
アミルアミン(東京化成工業株式会社製)0.1100gとイオン交換水9.9165gとの混合液を20mLガラス容器に0.9649gはかり採り、次いで実施例41で得られた分散液B20.0474gを加え、室温で2時間攪拌して分散液を得た。この分散液は安定で沈殿が生じることはなく、この分散液から得られた導電膜の電気伝導度は13S/cmであった。仕込み割合から計算された導電性高分子成分に対するそれ以外の成分の重量比は3.2であった。
ヘプチルアミン(東京化成工業株式会社製)0.0167gとイオン交換水6.2300gとの混合液を20mLガラス容器に5.2929gはかり採り、次いで実施例41で得られた分散液B20.5180gを加え、室温で2時間攪拌して分散液を得た。この分散液は安定で沈殿が生じることはなく、この分散液から得られた導電膜の電気伝導度は6S/cmであった。仕込み割合から計算された導電性高分子成分に対するそれ以外の成分の重量比は3.3であった。
Claims (24)
- 下記一般式(1)で表されるビニルスルホン酸類ユニットを含むポリビニルスルホン酸であって、
ビニルスルホン酸類モノマー由来のスルホン酸基のモル量が全モノマーユニットのモル量に対して50.0~98.0mol%であり、波長255~800nmの範囲で0.1以上の吸光度(水溶液0.2質量%、セル長10mm)を有するポリビニルスルホン酸。 - 重量平均分子量が10,000~800,000である請求項1に記載のポリビニルスルホン酸。
- 分子量が5,000以下の成分の含有率が10%以下である請求項1又は2に記載のポリビニルスルホン酸。
- 波長475~575nmの範囲で0.1以上の吸光度(水溶液0.2質量%、セル長10mm)を有する請求項1~3のいずれか一項に記載のポリビニルスルホン酸。
- 前記加熱する工程において、加熱温度が90~120℃であり、加熱時間が0.5~500時間の範囲である請求項5に記載のポリビニルスルホン酸の製造方法。
- 前記加熱する工程において、前記ポリビニルスルホン酸が溶媒類と混合した混合物の状態である請求項5又は6に記載のポリビニルスルホン酸の製造方法。
- 請求項1~4のいずれか一項に記載のポリビニルスルホン酸と導電性高分子とを含む複合体。
- 請求項8に記載の複合体を溶媒中に分散させてなる分散液。
- 請求項1~4のいずれか一項に記載のポリビニルスルホン酸を溶媒中に溶解及び/又は分散させ、該溶解及び/又は分散している溶媒中で、導電性高分子のモノマー類を重合させる工程を含む請求項9に記載の分散液の製造方法。
- 前記重合させる工程で得られた重合生成物を固体で取り出し当該固体を洗浄する工程、並びに
前記洗浄する工程後の固体を溶媒中に溶解及び/又は分散させる工程
を更に含む請求項10に記載の分散液の製造方法。 - 請求項9に記載の分散液を用いて製造された導電膜。
- 請求項12に記載の導電膜を含むコンデンサー。
- 請求項12に記載の導電膜を含む導電性フィルム又は導電性シート。
- ポリ(3,4―エチレンジオキシチオフェン)を含み、
反射法XDR測定において2θが8°~10°の範囲のピークKと2θが24°~28°の範囲のピークLとのピーク面積比(ピークKの面積/ピークLの面積)が1.0~10.0である導電膜。 - 導電膜を形成する分散液であって、
前記導電膜が、ポリ(3,4―エチレンジオキシチオフェン)を含み、
前記導電膜の反射法XDR測定において2θが8°~10°の範囲のピークKと2θが24°~28°の範囲のピークLとのピーク面積比(ピークKの面積/ピークLの面積)が1.0~10.0である、分散液。 - 導電性高分子及びポリアニオンを含む請求項16に記載の分散液。
- 前記導電性高分子がポリ(3,4―エチレンジオキシチオフェン)である請求項17に記載の分散液。
- 前記ポリアニオンが請求項1~4のいずれか一項に記載のポリビニルスルホン酸である請求項17に記載の分散液。
- 請求項16~19のいずれか一項に記載の分散液から形成される導電膜。
- ポリアニオンを溶媒中に溶解及び/又は分散させ、該溶解及び/又は分散している溶媒中で、導電性高分子のモノマー類を重合させる工程を含む請求項16~19のいずれか一項に記載の分散液の製造方法。
- 前記重合させる工程で得られた重合生成物を固体で取り出し当該固体を洗浄する工程、並びに
前記洗浄する工程後の固体を溶媒中に溶解及び/又は分散させる工程
を更に含む請求項21に記載の分散液の製造方法。 - 請求項15又は20に記載の導電膜を含むコンデンサー。
- 請求項15又は20に記載の導電膜を含む導電性フィルム又は導電性シート。
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JP2014157914A (ja) * | 2013-02-15 | 2014-08-28 | Toyo Ink Sc Holdings Co Ltd | 熱電変換素子用組成物およびその用途 |
JP2014199836A (ja) * | 2013-03-29 | 2014-10-23 | 東洋インキScホールディングス株式会社 | 熱電変換材料、熱電変換素子用組成物、熱電変換膜およびそれらを用いた熱電変換素子 |
JP2018006643A (ja) * | 2016-07-06 | 2018-01-11 | 信越ポリマー株式会社 | キャパシタの製造方法 |
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CN108137753B (zh) | 2016-01-04 | 2020-12-01 | 三菱化学株式会社 | 丙烯酸系聚合物颗粒及其制造方法、油墨组合物以及涂料组合物 |
KR102655243B1 (ko) | 2022-06-09 | 2024-04-08 | 주식회사 디스피스 | 적층식 조리기구 세트 |
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RU2560875C2 (ru) | 2015-08-20 |
JPWO2012147872A1 (ja) | 2014-07-28 |
CN103492424B (zh) | 2016-03-16 |
TW201307428A (zh) | 2013-02-16 |
EP2703417B1 (en) | 2017-02-22 |
TW201437250A (zh) | 2014-10-01 |
TWI466918B (zh) | 2015-01-01 |
EP2703417A4 (en) | 2015-07-15 |
EP2703417A1 (en) | 2014-03-05 |
RU2013147829A (ru) | 2015-06-10 |
US9321863B2 (en) | 2016-04-26 |
JP5758990B2 (ja) | 2015-08-05 |
TWI512001B (zh) | 2015-12-11 |
CN103492424A (zh) | 2014-01-01 |
KR20140000339A (ko) | 2014-01-02 |
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