[go: up one dir, main page]

WO2007074901A1 - Aqueous fluoropolymer dispersion - Google Patents

Aqueous fluoropolymer dispersion Download PDF

Info

Publication number
WO2007074901A1
WO2007074901A1 PCT/JP2006/326246 JP2006326246W WO2007074901A1 WO 2007074901 A1 WO2007074901 A1 WO 2007074901A1 JP 2006326246 W JP2006326246 W JP 2006326246W WO 2007074901 A1 WO2007074901 A1 WO 2007074901A1
Authority
WO
WIPO (PCT)
Prior art keywords
fluorine
fluoropolymer
aqueous
surfactant
dispersion
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Ceased
Application number
PCT/JP2006/326246
Other languages
French (fr)
Japanese (ja)
Inventor
Nobuhiko Tsuda
Chie Sawauchi
Hiromichi Momose
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Daikin Industries Ltd
Original Assignee
Daikin Industries Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Daikin Industries Ltd filed Critical Daikin Industries Ltd
Priority to JP2007521728A priority Critical patent/JP4985399B2/en
Publication of WO2007074901A1 publication Critical patent/WO2007074901A1/en
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09DCOATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
    • C09D127/00Coating 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 halogen; Coating compositions based on derivatives of such polymers
    • C09D127/02Coating 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 halogen; Coating compositions based on derivatives of such polymers not modified by chemical after-treatment
    • C09D127/12Coating 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 halogen; Coating compositions based on derivatives of such polymers not modified by chemical after-treatment containing fluorine atoms
    • C09D127/18Homopolymers or copolymers of tetrafluoroethene

Definitions

  • the present invention relates to an aqueous fluoropolymer dispersion.
  • Patent Document 1 uses an ethoxylated aliphatic alcohol type nonionic surfactant as a dispersant in a dispersion having an average particle size of 0.25 i um polytetrafluoroethylene [PTFE] particles. By doing so, it is described that the generation of sludge near room temperature can be suppressed.
  • PTFE polytetrafluoroethylene
  • Patent Document 2 (1) an aqueous dispersion of PTFE is concentrated by an ultrafiltration method, a fluorine-containing surfactant is added in an amount of 0 to 0.1% by weight, and a stabilizing emulsifier is added.
  • Patent Document 3 and Patent Document 4 disclose aqueous fluoropolymer dispersions with reduced PFOA. These references point out the problem of increasing the viscosity of the resulting fluoropolymer aqueous dispersion when PFOA is reduced. To overcome this problem, non-fluorine-based surfactants are added to fluoropolymers 1 to 1. A method of adding in the range of 12% has been proposed.
  • Patent Document 5 describes an aqueous PTFE dispersion in which the amount of a non-ionic surfactant is 1.5 to 4% by weight of PTFE particles. However, there is no specific description regarding the content of the fluorine-containing surfactant in this PTFE aqueous dispersion.
  • Patent Document 6 describes a method of obtaining a fluoropolymer aqueous dispersion by adding a nonionic emulsifier and removing the fluorine-containing emulsifier by contacting with an anion exchanger. However, this method has a problem that the fluoropolymer in the obtained aqueous fluoropolymer dispersion is not highly concentrated and is not practical.
  • Patent Document 1 Japanese Patent Application Laid-Open No. 47-6539
  • Patent Document 2 JP-A-55-120630
  • Patent Document 3 US Patent Application Publication No. 2004Z171736
  • Patent Document 4 US Patent Application Publication No. 2004Z186219
  • Patent Document 5 JP 2000-160118 A
  • Patent Document 6 Special Table 2002-532583 ([Claims], [0025]) Disclosure of Invention
  • the object of the present invention is to suppress the increase in viscosity due to an increase in the liquid temperature despite the low fluorine-containing surfactant concentration and the fluorine-free surfactant concentration, and is excellent in storage stability. It is to provide an aqueous fluoropolymer dispersion.
  • the present invention relates to a fluoropolymer aqueous dispersion in which particles comprising a fluoropolymer are dispersed in an aqueous medium in the presence of a fluorine-free surfactant, and the particles comprising the fluoropolymer are composed of the fluoropolymer aqueous solution.
  • the fluoropolymer is an aqueous fluoropolymer dispersion characterized in that the amount corresponds to 1% by mass or more and 5% by mass or less of the solid content of the fluoropolymer, and the fluoropolymer is modified polytetrafluoroethylene.
  • the aqueous fluoropolymer dispersion of the present invention is one in which particles having a fluoropolymer force are dispersed in an aqueous medium in the presence of a fluorine-free nonionic surfactant.
  • the fluoropolymer is a modified polytetra Fluoroethylene [modified PTFE].
  • the modified PTFE means a copolymer of TFE and a small amount of monomer other than TFE, which is non-melt processable.
  • the trace monomer examples include fluoroolefins such as HFP and CTFE, fluoro having an alkyl group having 1 to 5 carbon atoms, particularly 1 to 3 carbon atoms (alkyl butyl etherol); Rosioxol; perfluoroalkylethylene; ⁇ -hydroperfluoroolefin.
  • fluoroolefins such as HFP and CTFE
  • fluoro having an alkyl group having 1 to 5 carbon atoms, particularly 1 to 3 carbon atoms alkyl butyl etherol
  • Rosioxol perfluoroalkylethylene
  • ⁇ -hydroperfluoroolefin examples include fluoroolefins such as HFP and CTFE, fluoro having an alkyl group having 1 to 5 carbon atoms, particularly 1 to 3 carbon atoms (alkyl butyl etherol); Rosioxol; perfluoroalkylethylene; ⁇ -hydroper
  • the very small proportion monomer content ⁇ the total monomer units of the very small proportion monomer units derived from or, usually 0.001 to 1 Monore 0/0, preferably ⁇ or 0.005 to 0. 5 Monore 0/0, the more favorable Mashiku in the range of 0.01 to 0.1 Monore 0/0.
  • the content (mol%) of a trace monomer unit in all monomer units means the monomer from which the above “all monomer units” is derived, that is, a fluoropolymer. This means the mole fraction (mol%) of the trace monomer from which the trace monomer unit is derived, based on the total amount of the monomer that constitutes.
  • the average particle size of the fluoropolymer particles is 50 to 400 nm, preferably 100 to 350 nm.
  • the average particle size is determined by measuring the transmittance of the 550 nm projection light with respect to the unit length of the aqueous dispersion with the fluoropolymer particle concentration adjusted to 0.22 mass%, and the directional direction diameter in the transmission electron micrograph.
  • the permeability power is determined based on a calibration curve with the average particle diameter determined in the above.
  • the aqueous fluoropolymer dispersion of the present invention has a fluoropolymer particle strength of 35 to 70% by mass of the aqueous fluoropolymer dispersion.
  • the preferred lower limit of the content of the fluoropolymer particles in the aqueous fluoropolymer dispersion is 40% by mass, a more preferred lower limit is 50% by mass, and a preferred upper limit is 65% by mass.
  • the content of the fluoropolymer particles is based on the heating residue (Z) obtained by taking about 1 lg (X) of a sample in an aluminum cup with a diameter of 5 cm, drying at 100 ° C for 1 hour, and further drying at 300 ° C for 1 hour.
  • Formula: P ZZXX 100 (%)
  • the aqueous medium in the present invention is not particularly limited as long as it is a liquid containing water, and in addition to water, for example, a fluorine-free organic solvent such as alcohol, ether, ketone, paraffin wax, and Z or fluorine-containing organic It may also contain a solvent.
  • the aqueous fluoropolymer dispersion of the present invention may have a fluorine-free surfactant as a surfactant within the range described below.
  • the aqueous fluoropolymer dispersion may contain only one kind of the above non-fluorine-containing surfactant, or may contain two or more kinds! /.
  • the fluorine-free surfactant may be either a non-one surfactant or a char-on surfactant as long as it has a compound power not containing fluorine. It is preferably a non-ionic surfactant.
  • the non-ionic surfactant is not particularly limited as long as it is a non-ionic compound containing no fluorine (non-fluorine-containing non-ionic surfactant), and a known one is used. Can be used.
  • nonionic surfactant examples include ether type nonionic surfactants such as polyoxyethylene alkyl phenyl ether, polyoxyethylene alkyl ether, polyoxyethylene alkylene alkyl ether, and the like; ethylene oxide Z propylene Polyoxyethylene derivatives such as oxide block copolymers; sorbitan fatty acid esters
  • Ester-type surfactants such as polyoxyethylene sorbitan fatty acid ester, polyoxyethylene sorbitol fatty acid ester, glycerin fatty acid ester, polyoxyethylene fatty acid ester; polyoxyethylene alkylamine, alkyl alkanolamide, etc. Amine noion surfactants; and the like.
  • the hydrophobic group may be any of an alkylphenol group, a linear alkyl group, and a branched alkyl group, but the alkylphenol group is present in the structure. However, it is preferable that the compound does not have a benzene ring.
  • nonionic surfactants polyoxyethylene alkyl ether type nonionic surfactants are preferred.
  • the polyoxyethylene alkyl ether type non-ionic surfactant has 1 carbon atom. Those having a polyoxyethylene alkyl ether structure having an alkyl group of 0 to 20 are preferred, and those having a polyoxyethylene alkyl ether structure having an alkyl group having 10 to 15 carbon atoms are more preferred.
  • the alkyl group in the polyoxyethylene alkyl ether structure preferably has a branched structure.
  • polyoxyethylene alkyl ether type non-ionic surfactant examples include Genapol X080 (product name, manufactured by Clariant), Taditol 9—S-15 (product name, manufactured by Clariant), Neugen TDS-80 ( Product name, manufactured by Daiichi Kogyo Seiyaku Co., Ltd.).
  • non-ionic surfactant examples include those having an ethylene oxide propylene oxide [EO-PO] block copolymer structure, which is known as a pull nick type surfactant.
  • the on-surfactants, EO content is preferably 30 to 90 wt%, more preferably 35 to 85 wt%, more preferably 40-60 weight 0 / It is 0 , and the average molecular weight force multiplier ⁇ is 1000 to 10000, more preferably ⁇ is 2000 to 9 000, and more preferably 4000 to 8000.
  • Examples of the pull-mouth nick type surfactant include Pluronic PE6800, Pluronic PE6400 (product name, manufactured by BASF), Genapol PF40, Genapol PF80 (product name, manufactured by Clariant), and the like.
  • fluorine-free surfactants in the present invention for example, alkylsulfonic acid and its salt, alkylsulfuric acid ester and its salt, alkylsulfosuccinic acid ester and its salt, oxyalkyl Sulfonated acids and their salts.
  • a non-fluorine-containing surfactant a combination of a nonionic surfactant and a cation surfactant improves the storage stability and improves the liquid temperature in the resulting aqueous dispersion. Can suppress the increase in viscosity.
  • the fluorine-free surfactant is an amount corresponding to 1% by mass or more and 5% by mass or less of the fluoropolymer.
  • the above-mentioned aqueous fluoropolymer dispersion has a fluorine-free surfactant amount within the above-mentioned range, and is stored without significantly impairing crack resistance and mechanical stability, although it is lower than conventional aqueous fluoropolymer dispersions. Good stability and increased liquid temperature Accordingly, the increase in viscosity can be suppressed.
  • the fluorine-free surfactant is preferably in an amount corresponding to 1 to 3.5% by mass of the particles having a fluoropolymer force.
  • the more preferable lower limit of the content of the fluorine-free surfactant in the aqueous fluoropolymer dispersion is an amount corresponding to 2% by mass of the particles made of the fluoropolymer.
  • the aqueous fluoropolymer dispersion of the present invention may contain a fluorine-containing surfactant.
  • the fluorine-containing surfactant is not particularly limited as long as it has the ability to contain a fluorine-containing compound and exhibits an emulsifying action.
  • the fluorine-containing compound to be constituted those having an average molecular weight of 1000 or less are preferably removed. In terms of ease, those having an average molecular weight of 500 or less are more preferred, and those having 5 to 12 carbon atoms are preferred.
  • fluorine-containing surfactants include those containing fluorine-containing compounds such as fluorine-containing carboxylic acid compounds and fluorine-containing sulfonic acid compounds (hereinafter referred to as "fluorine-containing surfactant activities"). Fluorine-containing carboxylic acid compounds and cocoons or their salts are more preferred.
  • perfluorooctanoic acid and ⁇ or a salt thereof are collectively abbreviated as “PFOA”.
  • perfluorooctylsulfonic acid and Z or a salt thereof may be abbreviated as “PFOS”.
  • the fluorosurfactant is preferably perfluorocarboxylic acid and Z or a salt thereof.
  • examples of the counter ion forming the salt include alkali metal ions or NH +, and examples of the alkali metal ion include Na +, Ka +, etc.
  • NH + is preferable.
  • PFOS is a salt
  • examples thereof include an ammonium salt.
  • the amount of the fluorine-containing surfactant is not more than the amount corresponding to 50 ppm of the fluoropolymer.
  • the concentration of the fluorine-containing surfactant is preferably not more than an amount corresponding to 20 ppm, more preferably not more than an amount corresponding to 10 ppm.
  • the content of the fluorine-containing surfactant is determined by performing high-performance liquid chromatography [HPLC] under the conditions described below after adding Soxhlet extraction with the same amount of methanol as the aqueous fluoropolymer dispersion. It is measured by.
  • the aqueous fluoropolymer dispersion of the present invention is obtained by (1) polymerizing a fluoropolymer and (2) adjusting the respective contents of the fluoropolymer, the fluorine-containing surfactant and the fluorine-free surfactant. Can do.
  • the step (1) can be performed by a known method such as suspension polymerization or emulsion polymerization.
  • fluorine-containing monomer non-fluorine-containing monomer, and additives such as a polymerization initiator and a chain transfer agent used in each of the above polymerizations, known ones can be used as appropriate.
  • surfactants can be used.
  • each of the above polymerizations is preferably carried out in the presence of the above-mentioned fluorine-containing surfactant in an amount of from 0.0001 to LO mass% of the aqueous medium.
  • the amount of the fluorine-containing surfactant is preferably 0.001% by mass or more of the aqueous medium, more preferably 1% by mass or more.
  • step (2) depending on the amount of the fluorine-containing surfactant used in the step (1), the content of the fluoropolymer in the fluoropolymer dispersion obtained from the step (1), etc.
  • the means, conditions, etc. can be selected as appropriate.
  • the contents of the fluoropolymer and the fluorine-containing surfactant are the phase separation method described in the pamphlet of International Publication No. 2004Z050719, the ion exchange resin method described in JP 2002-532583 A, It can be adjusted by performing a conventionally known operation such as a membrane treatment method described in 55-120630, an electrophoresis method described in UK Patent No. 642025, an evaporation method described in JP 2003-531232, etc. Aqueous, but can be obtained
  • the amount of non-fluorine containing surfactant used in each operation must be limited so that the amount of non-fluorine containing surfactant in the dispersion does not exceed the scope of this application.
  • each operation may be performed once or may be performed twice or more.
  • the same operation may be repeated, You can combine different operations.
  • the content of the non-fluorine-containing surfactant is, for example, after the above-described operation, which limits the amount of the non-fluorine-containing surfactant used in each of the above-mentioned operations. It can be prepared by adding a fluorine-free surfactant.
  • the aqueous fluoropolymer dispersion of the present invention has a mechanical stability with a good dispersion stability despite the extremely low content of fluorine-containing surfactants and fluorine-free surfactants and high fluoropolymer concentration. Excellent in stability and storage stability.
  • the above fluoropolymer mono-aqueous dispersion has an extremely low content of each of the above-mentioned surfactants, the crack resistance and mechanical stability are not greatly impaired, it has excellent storage stability, and the liquid temperature. The increase in viscosity associated with the increase can be suppressed.
  • the above fluoropolymer aqueous dispersion contains the above-mentioned surfactant as a fluorine-free surfactant, it is particularly excellent in storage stability and can easily suppress an increase in viscosity accompanying an increase in liquid temperature.
  • the aqueous fluoropolymer dispersion of the present invention can be processed into, for example, a fluoropolymer powder, a molded article and the like.
  • the fluoropolymer powder has a very low content of the fluorine-containing surfactant, and thus is useful as an excellent molded material.
  • the fluoropolymer powder can be prepared by a conventional method according to the desired use.
  • aqueous fluoropolymer dispersion of the present invention can be coated on a coating, cast film, impregnated body or the like as it is or with various additives.
  • the above fluoropolymer aqueous dispersion is, for example, an oven lining, cooking utensils such as ice trays, electric wires, pipes, ship bottoms, high-frequency printed circuit boards, conveyor belts, coating materials on iron bottom plates; fiber base materials, woven fabrics / nonwoven fabrics, etc. Can be processed into an impregnated material, etc.
  • the fiber substrate is not particularly limited. For example, glass fiber, carbon fiber, And aramid fibers (Kepler (registered trademark) fibers, etc.).
  • Processing of the aqueous fluoropolymer dispersion can be performed by a conventionally known method.
  • the aqueous fluoropolymer dispersion of the present invention has the above-described configuration, the content of the fluorine-containing surfactant and the fluorine-free surfactant is extremely low, and the fluoropolymer mono has a high concentration. Furthermore, it is excellent in dispersion stability and storage stability, and can suppress an increase in viscosity accompanying an increase in liquid temperature.
  • Average particle size determined by measuring the transmittance of 550 nm projection light with respect to the unit length of an aqueous fluoropolymer dispersion adjusted to 0.22% by weight of the solid content of rosin and the directional direction diameter in a transmission electron micrograph Based on the calibration curve with the diameter, it was determined from the transmittance.
  • the obtained aqueous dispersion was added with an equal amount of methanol and subjected to Soxhlet extraction, and then subjected to high performance liquid chromatography [HPLC] under the following conditions.
  • HPLC high performance liquid chromatography
  • a calibration curve obtained by HPLC measurement with the above-mentioned eluate and conditions was used for a known concentration of the fluorine-containing surfactant.
  • fluoropolymer aqueous dispersion 50g was subjected to high-speed shearing with a homogenizer CM-1 00 (manufactured by Azwan Co., Ltd.) at 15000rpm for 5 minutes, and then filtered through a 400 mesh stainless steel wire mesh to collect the aggregates. Dry and weigh at 100 ° C.
  • the percentage of the aggregate relative to the fluoropolymer in the aqueous fluoropolymer dispersion was determined as mechanical stability. The smaller this value, the more stable the fluoropolymer aqueous dispersion is against shearing.
  • Degreased aluminum plate (size: 10cm x 15cm) is immersed in 100ml of fluoropolymer aqueous dispersion, dried at room temperature on a 45 ° slope for 5 minutes, further dried at 380 ° C for 10 minutes, and then cooled to room temperature Check for cracks with a 10X magnifier. Of the immersed aluminum plates that did not generate cracks, the maximum film thickness was measured with a film thickness meter to obtain CCT.
  • aqueous fluoropolymer dispersion 500 ml of an aqueous fluoropolymer dispersion was placed in a plastic container and allowed to stand in a temperature-controlled room at 25 ° C or 40 ° C for 2 months. After standing, the mixture was gently stirred and then filtered through a stainless steel 400 mesh, and the agglomerate remaining on the mesh was dried. Those with poor storage stability generate a large amount of agglomerates.
  • the temperature of the hot water bath was raised while stirring, the internal temperature reached 70 ° C, the stirring was stopped, the internal temperature was maintained at 70 ° C for 6 hours, and then the separated supernatant phase was removed, The PTFE aqueous dispersion phase was separated.
  • the resulting PTFE aqueous dispersion (concentrated aqueous dispersion) has a PTFE concentration of 70.5%, a fluorine-free surfactant content equivalent to 3.0% of PTFE, and a PFOA content of 48 ppm of PTFE. The amount was equivalent to
  • Neugen TDS-80 and ion-exchanged water are added to this aqueous dispersion to adjust the PTFE content to 60% and the fluorine-free surfactant to an amount equivalent to 6.0% of PTFE. It was.
  • Synthesis Example 1 The same as Synthesis Example 1 except that PTFE was changed to modified PTFE (perfluoropropyl butyl ether [PP VE] modified, modified amount 0.1 mol%, average particle size 240 nm) in Synthesis Example 1.
  • modified PTFE perfluoropropyl butyl ether [PP VE] modified, modified amount 0.1 mol%, average particle size 240 nm
  • PP VE perfluoropropyl butyl ether
  • PTFE dispersion (i) (PTFE content 30%, average particle diameter 220nm, PFOA content: PTFE equivalent to 2000ppm, fluorine-free surfactant (product name: Genapol X080, Clariant) content: An amount equivalent to 5% of PTFE) 2000g, an anion exchange resin (product name: Amberlite IRA402J, manufactured by Rohm 'And' Haas) 50ml in a column (diameter 2cm) filled with a temperature of 50 ° C, space Through the conditions of speed [SV] 2, the PTFE concentration is 30%, the fluorine-free surfactant content is equivalent to 4.9% of PTFE, and the PFOA content is equivalent to lOppm of PTFE. 1980 g of PTFE dispersion (ii) was obtained.
  • the PTFE aqueous dispersion separated from the PTFE aqueous dispersion phase has a PTFE concentration of 69.8%, a fluorine-free surfactant content, an amount equivalent to 2.5% of SpTFE, and a PFOA content of 2 ppm of PTFE. Is equivalent to o
  • Ion exchange water and Genapol X080 were added to this to adjust the amount of PTFE 60% and fluorine-free surfactant to 6% of PTFE.
  • ion exchange treatment and concentration were performed in the same manner as in Synthesis Example 4 to obtain a modified PTFE concentration of 70.5. %, A fluorine-free surfactant content corresponding to 2.5% of the modified PTFE, and a PFOA content corresponding to 2 ppm of the modified PTFE were obtained.
  • Ion exchange water and the above-mentioned non-fluorine-containing surfactant were added thereto, and the modified PTFE 60% and the content of non-fluorine-containing surfactant were adjusted to an amount corresponding to 6% of the modified PTFE.
  • Viscosity, mechanical stability, crack limit thickness [CCT] and storage stability were measured for the aqueous dispersions of each synthesis example.
  • Table 1 shows the measurement results.
  • the aqueous fluoropolymer dispersion of the present invention has the above-described configuration, the content of the fluorine-containing surfactant and the fluorine-free surfactant is extremely low, and the fluoropolymer mono has a high concentration. Furthermore, it is excellent in dispersion stability and storage stability, and can suppress an increase in viscosity accompanying an increase in liquid temperature.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Wood Science & Technology (AREA)
  • Organic Chemistry (AREA)
  • Compositions Of Macromolecular Compounds (AREA)

Abstract

The invention aims at providing an aqueous fluoropolymer dispersion which is suppressed in the viscosity increase due to liquid temperature rise and is therefore excellent in storage stability in spite of its low contents of a fluorinated surfactant and a fluorine-free surfactant. An aqueous fluoropolymer dispersion comprising an aqueous medium containing a fluorine-free surfactant and fluoropolymer particles dispersed therein, characterized in that the amount of the fluoropolymer particles is 35 to 70% by mass based on the dispersion, that the fluorinated surfactant content of the dispersion is 50ppm or below based on the amount of the fluoropolymer in terms of solid matter, that the content of the fluorinine-free surfactant is 1 to 5% by mass based on the amount of the fluoropolymer in terms of solid matter, and that the fluoropolymer is a modified polytetrafluoroethylene.

Description

明 細 書  Specification

フルォロポリマー水性分散液  Fluoropolymer aqueous dispersion

技術分野  Technical field

[0001] 本発明は、フルォロポリマー水性分散液に関する。  [0001] The present invention relates to an aqueous fluoropolymer dispersion.

背景技術  Background art

[0002] フルォロポリマー水性分散液において、従来より、フルォロポリマーの分散安定性、 貯蔵安定性等を維持する目的で各種界面活性剤が用いられている。  In aqueous fluoropolymer dispersions, various surfactants have heretofore been used for the purpose of maintaining the dispersion stability and storage stability of the fluoropolymer.

例えば、特許文献 1には、平均粒径 0. 25 iu mのポリテトラフルォロェチレン〔PTFE〕 粒子力 なる分散液においてエトキシィ匕脂肪族アルコール型のノ-オン界面活性剤 を分散剤として使用することにより、室温付近でのスラッジの生成が抑えられることが 記載されている。 For example, Patent Document 1 uses an ethoxylated aliphatic alcohol type nonionic surfactant as a dispersant in a dispersion having an average particle size of 0.25 i um polytetrafluoroethylene [PTFE] particles. By doing so, it is described that the generation of sludge near room temperature can be suppressed.

[0003] 特許文献 2には、(1)限外ろ過法によって、 PTFEの水性分散液を濃縮して、含フッ 素界面活性剤を固形分の 0〜0. 1重量%、安定化乳化剤を固形分の 0. 5〜5重量 %含む濃縮水性分散液、 (2) PTFE20重量%とパーフルォロオクタン酸アンモ-ゥ ム 0八〕0. 3%とを含む水性分散液に、アルキルフエノール構造を有する安定ィ匕 乳化剤の存在下で限外ろ過を行い濃縮することにより、該 PFOAの 98%を除去し、 PFOA量 60ppm、 PTFE濃度 59%の水性分散液を得る方法が記載されている。し 力しながら、この文献には、フルォロポリマー水性分散液中の PFOAを更に低減した 場合のフルォロポリマー水性分散液の安定性に関する記載はない。  [0003] In Patent Document 2, (1) an aqueous dispersion of PTFE is concentrated by an ultrafiltration method, a fluorine-containing surfactant is added in an amount of 0 to 0.1% by weight, and a stabilizing emulsifier is added. Concentrated aqueous dispersion containing 0.5 to 5% by weight of solids, (2) Alkylphenol in aqueous dispersion containing 20% by weight of PTFE and ammonium perfluorooctanoate 0.88] It describes a method for obtaining an aqueous dispersion having a PFOA amount of 60 ppm and a PTFE concentration of 59% by removing 98% of the PFOA by concentrating by ultrafiltration in the presence of a stable emulsifier having a structure. . However, this document does not describe the stability of the aqueous fluoropolymer dispersion when the PFOA in the aqueous fluoropolymer dispersion is further reduced.

[0004] 特許文献 3及び特許文献 4には、 PFOAを低減させたフルォロポリマー水性分散液 が開示されている。これらの文献では、 PFOAを低減した場合、得られるフルォロポリ マー水性分散液の粘度が上昇する問題が指摘され、この問題を克服するために非 フッ素系のァ-オン界面活性剤をフルォロポリマーの 1〜12%の範囲で添加する方 法が提案されている。  [0004] Patent Document 3 and Patent Document 4 disclose aqueous fluoropolymer dispersions with reduced PFOA. These references point out the problem of increasing the viscosity of the resulting fluoropolymer aqueous dispersion when PFOA is reduced. To overcome this problem, non-fluorine-based surfactants are added to fluoropolymers 1 to 1. A method of adding in the range of 12% has been proposed.

[0005] 特許文献 5には、ノ-オン界面活性剤量が PTFE粒子の 1. 5〜4重量%である PTF E水性分散液が記載されている。しかしながら、この PTFE水性分散液は、含フッ素 ァ-オン界面活性剤の含有量に関する具体的な記載はない。 [0006] 特許文献 6には、非イオン性乳化剤を加え、陰イオン交換体に接触させることによりフ ッ素含有乳化剤を除去してフルォロポリマー水性分散液を得る方法が記載されてい る。しかしながら、この方法では、得られるフルォロポリマー水性分散液におけるフル ォロポリマーは高濃度化されておらず、実用的でない問題がある。 [0005] Patent Document 5 describes an aqueous PTFE dispersion in which the amount of a non-ionic surfactant is 1.5 to 4% by weight of PTFE particles. However, there is no specific description regarding the content of the fluorine-containing surfactant in this PTFE aqueous dispersion. [0006] Patent Document 6 describes a method of obtaining a fluoropolymer aqueous dispersion by adding a nonionic emulsifier and removing the fluorine-containing emulsifier by contacting with an anion exchanger. However, this method has a problem that the fluoropolymer in the obtained aqueous fluoropolymer dispersion is not highly concentrated and is not practical.

特許文献 1:特開昭 47— 6539号公報  Patent Document 1: Japanese Patent Application Laid-Open No. 47-6539

特許文献 2:特開昭 55— 120630号公報  Patent Document 2: JP-A-55-120630

特許文献 3 :米国特許出願公開第 2004Z171736号明細書  Patent Document 3: US Patent Application Publication No. 2004Z171736

特許文献 4:米国特許出願公開第 2004Z186219号明細書  Patent Document 4: US Patent Application Publication No. 2004Z186219

特許文献 5 :特開 2000— 160118号公報  Patent Document 5: JP 2000-160118 A

特許文献 6:特表 2002— 532583号公報( [特許請求の範囲]、 [0025] ) 発明の開示  Patent Document 6: Special Table 2002-532583 ([Claims], [0025]) Disclosure of Invention

発明が解決しょうとする課題  Problems to be solved by the invention

[0007] 本発明の目的は、上記現状に鑑み、含フッ素界面活性剤濃度及びフッ素非含有界 面活性剤濃度が低いにもかかわらず液温上昇による粘度上昇を抑え、貯蔵安定性 に優れたフルォロポリマー水性分散液を提供することにある。 [0007] In view of the above situation, the object of the present invention is to suppress the increase in viscosity due to an increase in the liquid temperature despite the low fluorine-containing surfactant concentration and the fluorine-free surfactant concentration, and is excellent in storage stability. It is to provide an aqueous fluoropolymer dispersion.

課題を解決するための手段  Means for solving the problem

[0008] 本発明は、フッ素非含有界面活性剤の存在下に水性媒体中にフルォロポリマーから なる粒子が分散して 、るフルォロポリマー水性分散液であって、上記フルォロポリマ 一からなる粒子は、上記フルォロポリマー水性分散液の 35〜70質量%であり、上記 フルォロポリマー水性分散液中における含フッ素界面活性剤は、上記フルォロポリマ 一の固形分の 50ppmに相当する量以下であり、上記フッ素非含有界面活性剤は、 上記フルォロポリマーの固形分の 1質量%以上、 5質量%以下に相当する量であり、 上記フルォロポリマーは、変性ポリテトラフルォロエチレンであることを特徴とするフル ォロポリマー水性分散液である。  [0008] The present invention relates to a fluoropolymer aqueous dispersion in which particles comprising a fluoropolymer are dispersed in an aqueous medium in the presence of a fluorine-free surfactant, and the particles comprising the fluoropolymer are composed of the fluoropolymer aqueous solution. 35 to 70% by mass of the dispersion, and the fluorine-containing surfactant in the aqueous fluoropolymer dispersion is below the amount corresponding to 50 ppm of the solid content of the fluoropolymer, and the fluorine-free surfactant is The fluoropolymer is an aqueous fluoropolymer dispersion characterized in that the amount corresponds to 1% by mass or more and 5% by mass or less of the solid content of the fluoropolymer, and the fluoropolymer is modified polytetrafluoroethylene.

以下に本発明を詳細に説明する。  The present invention is described in detail below.

[0009] 本発明のフルォロポリマー水性分散液は、フッ素非含有ノ-オン界面活性剤の存在 下に水性媒体中にフルォロポリマー力 なる粒子が分散して 、るものである。  [0009] The aqueous fluoropolymer dispersion of the present invention is one in which particles having a fluoropolymer force are dispersed in an aqueous medium in the presence of a fluorine-free nonionic surfactant.

上記フルォロポリマー水性分散液において、上記フルォロポリマーは、変性ポリテトラ フルォロエチレン〔変性 PTFE〕である。 In the aqueous fluoropolymer dispersion, the fluoropolymer is a modified polytetra Fluoroethylene [modified PTFE].

上記変性 PTFEとは、 TFEと、 TFE以外の微量単量体との共重合体であって、非溶 融加工性であるものを意味する。  The modified PTFE means a copolymer of TFE and a small amount of monomer other than TFE, which is non-melt processable.

上記微量単量体としては、例えば、 HFP、 CTFE等のフルォロォレフイン、炭素原子 1〜5個、特に炭素原子 1〜3個を有するアルキル基を持つフルォロ(アルキルビュル エーテノレ);フルォロジォキソール;パーフルォロアルキルエチレン; ω—ヒドロパーフ ルォロォレフイン等が挙げられる。  Examples of the trace monomer include fluoroolefins such as HFP and CTFE, fluoro having an alkyl group having 1 to 5 carbon atoms, particularly 1 to 3 carbon atoms (alkyl butyl etherol); Rosioxol; perfluoroalkylethylene; ω-hydroperfluoroolefin.

変性 PTFEにおいて、上記微量単量体に由来する微量単量体単位の全単量体単位 に占める含有率 ίま、通常 0. 001〜1モノレ0 /0、好ましく ίま 0. 005〜0. 5モノレ0 /0、より好 ましくは 0. 01〜0. 1モノレ0 /0の範囲である。 In the modified PTFE, the very small proportion monomer content ί the total monomer units of the very small proportion monomer units derived from or, usually 0.001 to 1 Monore 0/0, preferably ί or 0.005 to 0. 5 Monore 0/0, the more favorable Mashiku in the range of 0.01 to 0.1 Monore 0/0.

本明細書にぉ 、て、「全単量体単位に占める微量単量体単位の含有率 (モル%)」と は、上記「全単量体単位」が由来する単量体、即ち、フルォロポリマーを構成すること となった単量体全量に占める、上記微量単量体単位が由来する微量単量体のモル 分率 (モル%)を意味する。  In the present specification, “the content (mol%) of a trace monomer unit in all monomer units” means the monomer from which the above “all monomer units” is derived, that is, a fluoropolymer. This means the mole fraction (mol%) of the trace monomer from which the trace monomer unit is derived, based on the total amount of the monomer that constitutes.

[0010] 上記フルォロポリマー粒子の平均粒子径は、 50〜400nmであり、好ましくは、 100 〜350nmである。 [0010] The average particle size of the fluoropolymer particles is 50 to 400 nm, preferably 100 to 350 nm.

上記平均粒子径は、フルォロポリマー粒子の濃度を 0. 22質量%に調整した水性分 散液の単位長さに対する 550nmの投射光の透過率と、透過型電子顕微鏡写真に おける定方向径を測定して決定された平均粒子径との検量線をもとにして、上記透 過率力 決定したものである。  The average particle size is determined by measuring the transmittance of the 550 nm projection light with respect to the unit length of the aqueous dispersion with the fluoropolymer particle concentration adjusted to 0.22 mass%, and the directional direction diameter in the transmission electron micrograph. The permeability power is determined based on a calibration curve with the average particle diameter determined in the above.

[0011] 本発明のフルォロポリマー水性分散液は、フルォロポリマー粒子力 本フルォロポリ マー水性分散液の 35〜70質量%であるものである。 The aqueous fluoropolymer dispersion of the present invention has a fluoropolymer particle strength of 35 to 70% by mass of the aqueous fluoropolymer dispersion.

上記フルォロポリマー水性分散液におけるフルォロポリマー粒子の含有量は、好まし い下限が 40質量%、より好ましい下限が 50質量%であり、好ましい上限が 65質量% である。  The preferred lower limit of the content of the fluoropolymer particles in the aqueous fluoropolymer dispersion is 40% by mass, a more preferred lower limit is 50% by mass, and a preferred upper limit is 65% by mass.

上記フルォロポリマー粒子の含有量は、試料約 lg (X)を直径 5cmのアルミカップに とり、 100°C、 1時間で乾燥し、更に 300°C、 1時間乾燥した加熱残分 (Z)に基づき、 式: P=ZZXX 100 (%)にて決定したものである。 [0012] 本発明における水性媒体は、水を含む液体であれば特に限定されず、水に加え、例 えば、アルコール、エーテル、ケトン、パラフィンワックス等のフッ素非含有有機溶媒 及び Z又はフッ素含有有機溶媒をも含むものであってもよい。 The content of the fluoropolymer particles is based on the heating residue (Z) obtained by taking about 1 lg (X) of a sample in an aluminum cup with a diameter of 5 cm, drying at 100 ° C for 1 hour, and further drying at 300 ° C for 1 hour. Formula: P = ZZXX 100 (%) [0012] The aqueous medium in the present invention is not particularly limited as long as it is a liquid containing water, and in addition to water, for example, a fluorine-free organic solvent such as alcohol, ether, ketone, paraffin wax, and Z or fluorine-containing organic It may also contain a solvent.

[0013] 本発明のフルォロポリマー水性分散液は、界面活性剤としてフッ素非含有界面活性 剤を後述の範囲内で有し得るものである。 [0013] The aqueous fluoropolymer dispersion of the present invention may have a fluorine-free surfactant as a surfactant within the range described below.

上記フルォロポリマー水性分散液は、上記フッ素非含有界面活性剤を 1種のみ含有 するものであってもよ 、し、 2種以上含有するものであってもよ!/、。  The aqueous fluoropolymer dispersion may contain only one kind of the above non-fluorine-containing surfactant, or may contain two or more kinds! /.

[0014] 上記フッ素非含有界面活性剤としては、フッ素を含有していない化合物力 なるもの であれば、ノ-オン界面活性剤であってもよ 、しァ-オン界面活性剤であってもよ ヽ 力 ノ-オン界面活性剤であることが好ましい。 [0014] The fluorine-free surfactant may be either a non-one surfactant or a char-on surfactant as long as it has a compound power not containing fluorine. It is preferably a non-ionic surfactant.

[0015] 上記ノ-オン界面活性剤としては、フッ素を含有しないノ-オン性の化合物からなる もの(フッ素非含有ノ-オン界面活性剤)であれば特に限定されず、公知のものを使 用できる。 [0015] The non-ionic surfactant is not particularly limited as long as it is a non-ionic compound containing no fluorine (non-fluorine-containing non-ionic surfactant), and a known one is used. Can be used.

上記ノ-オン界面活性剤としては、例えば、ポリオキシエチレンアルキルフエニルェ 一テル、ポリオキシエチレンアルキルエーテル、ポリオキシエチレンアルキレンアルキ ルエーテル等のエーテル型ノ-オン界面活性剤;エチレンオキサイド Zプロピレンォ キサイドブロック共重合体等のポリオキシエチレン誘導体;ソルビタン脂肪酸エステル Examples of the nonionic surfactant include ether type nonionic surfactants such as polyoxyethylene alkyl phenyl ether, polyoxyethylene alkyl ether, polyoxyethylene alkylene alkyl ether, and the like; ethylene oxide Z propylene Polyoxyethylene derivatives such as oxide block copolymers; sorbitan fatty acid esters

、ポリオキシエチレンソルビタン脂肪酸エステル、ポリオキシエチレンソルビトール脂 肪酸エステル、グリセリン脂肪酸エステル、ポリオキシエチレン脂肪酸エステル等のェ ステル型ノ-オン界面活性剤;ポリオキシエチレンアルキルァミン、アルキルアルカノ ールアミド等のアミン系ノユオン界面活性剤;等が挙げられる。 Ester-type surfactants such as polyoxyethylene sorbitan fatty acid ester, polyoxyethylene sorbitol fatty acid ester, glycerin fatty acid ester, polyoxyethylene fatty acid ester; polyoxyethylene alkylamine, alkyl alkanolamide, etc. Amine noion surfactants; and the like.

[0016] 上記ノ-オン界面活性剤を構成する化合物において、その疎水基は、アルキルフエ ノール基、直鎖アルキル基及び分岐アルキル基の何れであってもよいが、アルキル フエノール基を構造中に有しな 、化合物等、ベンゼン環を有さな 、ものであることが 好ましい。  [0016] In the compound constituting the above-described surfactant, the hydrophobic group may be any of an alkylphenol group, a linear alkyl group, and a branched alkyl group, but the alkylphenol group is present in the structure. However, it is preferable that the compound does not have a benzene ring.

[0017] 上記ノ-オン界面活性剤としては、なかでも、ポリオキシエチレンアルキルエーテル 型ノニオン界面活性剤が好まし 、。  [0017] Among the above-mentioned nonionic surfactants, polyoxyethylene alkyl ether type nonionic surfactants are preferred.

上記ポリオキシエチレンアルキルエーテル型ノ-オン界面活性剤としては、炭素数 1 0〜20のアルキル基を有するポリオキシエチレンアルキルエーテル構造からなるもの が好ましく、炭素数 10〜 15のアルキル基を有するポリオキシエチレンアルキルエー テル構造力もなるものがより好まし 、。上記ポリオキシエチレンアルキルエーテル構 造におけるアルキル基は、分岐構造を有して 、ることが好まし 、。 The polyoxyethylene alkyl ether type non-ionic surfactant has 1 carbon atom. Those having a polyoxyethylene alkyl ether structure having an alkyl group of 0 to 20 are preferred, and those having a polyoxyethylene alkyl ether structure having an alkyl group having 10 to 15 carbon atoms are more preferred. The alkyl group in the polyoxyethylene alkyl ether structure preferably has a branched structure.

上記ポリオキシエチレンアルキルエーテル型ノ-オン界面活性剤としては、例えば、 Genapol X080 (製品名、クラリアント社製)、タージトール 9— S— 15 (製品名、クラ リアント社製)、ノィゲン TDS— 80 (製品名、第一工業製薬社製)等が挙げられる。 上記ノ-オン界面活性剤としては、更に、プル口ニック型界面活性剤として知られる エチレンオキサイド プロピレンオキサイド〔EO— PO]ブロック共重合体構造を有す るものが挙げられる。  Examples of the polyoxyethylene alkyl ether type non-ionic surfactant include Genapol X080 (product name, manufactured by Clariant), Taditol 9—S-15 (product name, manufactured by Clariant), Neugen TDS-80 ( Product name, manufactured by Daiichi Kogyo Seiyaku Co., Ltd.). Examples of the non-ionic surfactant include those having an ethylene oxide propylene oxide [EO-PO] block copolymer structure, which is known as a pull nick type surfactant.

上記 EO— POブロック共重合体構造を有するノ-オン界面活性剤としては、 EO含有 量が好ましくは 30〜90重量%、より好ましくは 35〜85重量%、更に好ましくは 40〜 60重量0 /0であり、平均分子量力 子まし <は 1000〜10000、より好まし <は 2000〜9 000、更に好ましくは 4000〜8000のものが挙げられる。上記プル口ニック型界面活 性剤としては、例えば、 Pluronic PE6800、 Pluronic PE6400 (製品名、 BASF 社製)、 Genapol PF40、 Genapol PF80 (製品名、クラリアント社製)等が挙げら れる。 The EO-PO Roh having a block copolymer structure - The on-surfactants, EO content is preferably 30 to 90 wt%, more preferably 35 to 85 wt%, more preferably 40-60 weight 0 / It is 0 , and the average molecular weight force multiplier <is 1000 to 10000, more preferably <is 2000 to 9 000, and more preferably 4000 to 8000. Examples of the pull-mouth nick type surfactant include Pluronic PE6800, Pluronic PE6400 (product name, manufactured by BASF), Genapol PF40, Genapol PF80 (product name, manufactured by Clariant), and the like.

[0018] 本発明におけるフッ素非含有界面活性剤のうち、ァ-オン界面活性剤としては、例え ば、アルキルスルホン酸及びその塩、アルキル硫酸エステル及びその塩、アルキルス ルホコハク酸エステル及びその塩、ォキシアルキル化されたスルホン酸及びその塩 等が挙げられる。上記フッ素非含有界面活性剤として、ノ-オン界面活性剤とァ-ォ ン界面活性剤とを併用することにより、得られる水性分散液において、効率よぐ貯蔵 安定性を向上させ、液温上昇に伴う粘度上昇を抑制することができる。  [0018] Among the fluorine-free surfactants in the present invention, as a surfactant, for example, alkylsulfonic acid and its salt, alkylsulfuric acid ester and its salt, alkylsulfosuccinic acid ester and its salt, oxyalkyl Sulfonated acids and their salts. As a non-fluorine-containing surfactant, a combination of a nonionic surfactant and a cation surfactant improves the storage stability and improves the liquid temperature in the resulting aqueous dispersion. Can suppress the increase in viscosity.

[0019] 本発明のフルォロポリマー水性分散液において、フッ素非含有界面活性剤は、フル ォロポリマーの 1質量%以上、 5質量%以下に相当する量である。  [0019] In the aqueous fluoropolymer dispersion of the present invention, the fluorine-free surfactant is an amount corresponding to 1% by mass or more and 5% by mass or less of the fluoropolymer.

上記フルォロポリマー水性分散液は、フッ素非含有界面活性剤量が上記範囲内に あり、従来一般のフルォロポリマー水性分散液よりも低いにもかかわらず、耐クラック 性及び機械的安定性を大きく損なうことなぐ貯蔵安定性が良好であり、液温上昇に よる粘度上昇を抑制することができる。 The above-mentioned aqueous fluoropolymer dispersion has a fluorine-free surfactant amount within the above-mentioned range, and is stored without significantly impairing crack resistance and mechanical stability, although it is lower than conventional aqueous fluoropolymer dispersions. Good stability and increased liquid temperature Accordingly, the increase in viscosity can be suppressed.

上記フッ素非含有界面活性剤は、フルォロポリマー力 なる粒子の 1〜3. 5質量% に相当する量であることが好ましい。  The fluorine-free surfactant is preferably in an amount corresponding to 1 to 3.5% by mass of the particles having a fluoropolymer force.

上記フルォロポリマー水性分散液におけるフッ素非含有界面活性剤の含有量は、よ り好ましい下限がフルォロポリマーからなる粒子の 2質量%に相当する量である。 本明細書において、上記フッ素非含有界面活性剤の含有量 (N)は、試料約 lg (Xg) を直径 5cmのアルミカップにとり、 100°Cにて 1時間で加熱した加熱残分 (Yg)、更に 、得られた加熱残分 (Yg)を 300°Cにて 1時間加熱した加熱残分 (Zg)より、式: N= [ (Y-Z) /Z] X 100 (%)から算出したものである。  The more preferable lower limit of the content of the fluorine-free surfactant in the aqueous fluoropolymer dispersion is an amount corresponding to 2% by mass of the particles made of the fluoropolymer. In this specification, the content (N) of the non-fluorine-containing surfactant is the residue of heating (Yg) obtained by taking about 1 lg (Xg) of a sample in an aluminum cup with a diameter of 5 cm and heating at 100 ° C for 1 hour. Furthermore, the heating residue (Yg) obtained was calculated from the heating residue (Zg) heated at 300 ° C for 1 hour from the formula: N = [(YZ) / Z] X 100 (%) It is.

[0020] 本発明のフルォロポリマー水性分散液は、含フッ素界面活性剤を含み得るものであ る。 [0020] The aqueous fluoropolymer dispersion of the present invention may contain a fluorine-containing surfactant.

上記含フッ素界面活性剤としては、含フッ素化合物力 なり乳化作用を示すものであ れば特に限定されないが、構成する含フッ素化合物としては、平均分子量が 1000以 下であるものが好ましぐ除去容易である点で、平均分子量が 500以下であるものが より好ましぐまた、炭素数が 5〜12であるものが好ましい。  The fluorine-containing surfactant is not particularly limited as long as it has the ability to contain a fluorine-containing compound and exhibits an emulsifying action. However, as the fluorine-containing compound to be constituted, those having an average molecular weight of 1000 or less are preferably removed. In terms of ease, those having an average molecular weight of 500 or less are more preferred, and those having 5 to 12 carbon atoms are preferred.

[0021] 上記含フッ素界面活性剤としては、含フッ素カルボン酸ィ匕合物、含フッ素スルホン酸 化合物等の含フッ素ァ-オンィ匕合物力 なるもの(以下、「含フッ素ァ-オン界面活 性剤」ということがある。)が好ましぐ含フッ素カルボン酸ィ匕合物及び Ζ又はその塩か らなるものがより好ましい。 [0021] The above-mentioned fluorine-containing surfactants include those containing fluorine-containing compounds such as fluorine-containing carboxylic acid compounds and fluorine-containing sulfonic acid compounds (hereinafter referred to as "fluorine-containing surfactant activities"). Fluorine-containing carboxylic acid compounds and cocoons or their salts are more preferred.

上記含フッ素ァ-オン化合物としては、例えば、パーフルォロオクタン酸及び Ζ又は その塩(以下、「パーフルォロオクタン酸及び Ζ又はその塩」をまとめて「PFOA」と略 記することがある。)、パーフルォロォクチルスルホン酸及び Z又はその塩(以下、「パ 一フルォロォクチルスルホン酸及び Z又はその塩」をまとめて「PFOS」と略記するこ とがある。)等が挙げられる。  As the fluorine-containing compound, for example, perfluorooctanoic acid and Ζ or a salt thereof (hereinafter, “perfluorooctanoic acid and Ζ or a salt thereof” are collectively abbreviated as “PFOA”. Perfluorooctylsulfonic acid and Z or a salt thereof (hereinafter, “perfluorooctylsulfonic acid and Z or a salt thereof” may be abbreviated as “PFOS”). Etc.

本発明において、上記含フッ素界面活性剤としては、パーフルォロカルボン酸及び Z又はその塩力 なるものが好まし 、。  In the present invention, the fluorosurfactant is preferably perfluorocarboxylic acid and Z or a salt thereof.

上記含フッ素ァ-オン化合物が塩である場合、該塩を形成する対イオンとしては、ァ ルカリ金属イオン又は NH +等が挙げられ、アルカリ金属イオンとしては、例えば、 Na +、 Ka+等が挙げられる。上記対イオンとしては、 NH +が好ましい。上記 PFOA及び When the fluorine-containing compound is a salt, examples of the counter ion forming the salt include alkali metal ions or NH +, and examples of the alkali metal ion include Na +, Ka +, etc. As the counter ion, NH + is preferable. PFOA and above

4  Four

PFOSは、塩である場合、特に限定されないが、アンモ-ゥム塩等が挙げられる。  When PFOS is a salt, it is not particularly limited, and examples thereof include an ammonium salt.

[0022] 本発明のフルォロポリマー水性分散液において、上記含フッ素界面活性剤は、フル ォロポリマーの 50ppmに相当する量以下である。 [0022] In the aqueous fluoropolymer dispersion of the present invention, the amount of the fluorine-containing surfactant is not more than the amount corresponding to 50 ppm of the fluoropolymer.

上記含フッ素界面活性剤濃度は、好ましくは 20ppmに相当する量以下、より好ましく は lOppmに相当する量以下であってもよい。  The concentration of the fluorine-containing surfactant is preferably not more than an amount corresponding to 20 ppm, more preferably not more than an amount corresponding to 10 ppm.

本明細書において、含フッ素界面活性剤の含有量は、フルォロポリマー水性分散液 と等量のメタノールを添加してソックスレー抽出を行ったのち、後述の条件にて、高速 液体クロマトグラフィー〔HPLC〕を行うことにより測定したものである。  In the present specification, the content of the fluorine-containing surfactant is determined by performing high-performance liquid chromatography [HPLC] under the conditions described below after adding Soxhlet extraction with the same amount of methanol as the aqueous fluoropolymer dispersion. It is measured by.

[0023] 本発明のフルォロポリマー水性分散液は、(1)フルォロポリマーの重合を行い、 (2) フルォロポリマー、含フッ素界面活性剤及びフッ素非含有界面活性剤の各含有量を 調整すること〖こより得ることができる。 [0023] The aqueous fluoropolymer dispersion of the present invention is obtained by (1) polymerizing a fluoropolymer and (2) adjusting the respective contents of the fluoropolymer, the fluorine-containing surfactant and the fluorine-free surfactant. Can do.

[0024] 上記工程(1)は、懸濁重合、乳化重合等、公知の方法にて行うことができる。 [0024] The step (1) can be performed by a known method such as suspension polymerization or emulsion polymerization.

上記各重合において使用するフッ素含有単量体、フッ素非含有単量体、及び、重合 開始剤、連鎖移動剤等の添加剤として、適宜公知のものを使用することができ、また 、上記各重合において、上述の界面活性剤を使用することができる。  As the fluorine-containing monomer, non-fluorine-containing monomer, and additives such as a polymerization initiator and a chain transfer agent used in each of the above polymerizations, known ones can be used as appropriate. In the above-mentioned surfactants can be used.

上記各重合は、重合効率の点で、上述の含フッ素界面活性剤を上記水性媒体の 0. 0001〜: LO質量%の量存在させて行うことが好ましい。上記含フッ素界面活性剤の 量は、上記水性媒体の 0. 001質量%以上であることが好ましぐ 1質量%以上である ことがより好ましい。  From the viewpoint of polymerization efficiency, each of the above polymerizations is preferably carried out in the presence of the above-mentioned fluorine-containing surfactant in an amount of from 0.0001 to LO mass% of the aqueous medium. The amount of the fluorine-containing surfactant is preferably 0.001% by mass or more of the aqueous medium, more preferably 1% by mass or more.

[0025] 上記工程(2)は、上記工程(1)において使用した含フッ素界面活性剤の使用量、上 記工程(1)から得られるフルォロポリマー分散液のフルォロポリマーの含有量等に応 じて、その手段、条件等を適宜選択して行うことができる。  [0025] In the step (2), depending on the amount of the fluorine-containing surfactant used in the step (1), the content of the fluoropolymer in the fluoropolymer dispersion obtained from the step (1), etc. The means, conditions, etc. can be selected as appropriate.

上記工程(2)において、フルォロポリマー及び含フッ素界面活性剤の各含有量は、 国際公開第 2004Z050719号パンフレット記載の相分離法、特表 2002— 532583 号公報記載のイオン交換榭脂法、特開昭 55— 120630号公報記載の膜処理法、英 国特許第 642025号明細書記載の電気泳動法、特表 2003— 531232号公報記載 の蒸発法等、従来公知の操作を行うことにより調整することができるが、得られる水性 分散液においてフッ素非含有界面活性剤の量が本願の範囲を越えないよう、各操作 におけるフッ素非含有界面活性剤の使用量を限定しなければならない。 In the step (2), the contents of the fluoropolymer and the fluorine-containing surfactant are the phase separation method described in the pamphlet of International Publication No. 2004Z050719, the ion exchange resin method described in JP 2002-532583 A, It can be adjusted by performing a conventionally known operation such as a membrane treatment method described in 55-120630, an electrophoresis method described in UK Patent No. 642025, an evaporation method described in JP 2003-531232, etc. Aqueous, but can be obtained The amount of non-fluorine containing surfactant used in each operation must be limited so that the amount of non-fluorine containing surfactant in the dispersion does not exceed the scope of this application.

上記工程(2)において、各操作は 1回行うものであってもよいし 2回以上行うものであ つてもよく、また各操作を 2回以上行う場合、同じ操作を繰り返してもよいし、異なる操 作を組合せて行ってもょ ヽ。  In the above step (2), each operation may be performed once or may be performed twice or more. When each operation is performed twice or more, the same operation may be repeated, You can combine different operations.

[0026] 上記工程(2)において、フッ素非含有界面活性剤の含有量は、例えば、上述の各操 作において使用する上記フッ素非含有界面活性剤の量を限定する、上述の操作後 に含フッ素非含有界面活性剤を添加する、等により調製することができる。  [0026] In the step (2), the content of the non-fluorine-containing surfactant is, for example, after the above-described operation, which limits the amount of the non-fluorine-containing surfactant used in each of the above-mentioned operations. It can be prepared by adding a fluorine-free surfactant.

[0027] 本発明のフルォロポリマー水性分散液は、含フッ素界面活性剤及びフッ素非含有界 面活性剤の含有量が極めて低く且つフルォロポリマー濃度が高いにもかかわらず分 散安定性が良ぐ機械的安定性及び貯蔵安定性に優れている。上記フルォロポリマ 一水性分散液は、上記各界面活性剤の含有量が極めて低いにもかかわらず、耐クラ ック性及び機械的安定性が大きく損なわれておらず、貯蔵安定性に優れ、液温上昇 に伴う粘度上昇を抑制することができる。  [0027] The aqueous fluoropolymer dispersion of the present invention has a mechanical stability with a good dispersion stability despite the extremely low content of fluorine-containing surfactants and fluorine-free surfactants and high fluoropolymer concentration. Excellent in stability and storage stability. Although the above fluoropolymer mono-aqueous dispersion has an extremely low content of each of the above-mentioned surfactants, the crack resistance and mechanical stability are not greatly impaired, it has excellent storage stability, and the liquid temperature. The increase in viscosity associated with the increase can be suppressed.

上記フルォロポリマー水性分散液は、フッ素非含有界面活性剤として上述の界面活 性剤を含有する場合、特に貯蔵安定性に優れ、また液温上昇に伴う粘度上昇も容易 に抑制することができる。  When the above fluoropolymer aqueous dispersion contains the above-mentioned surfactant as a fluorine-free surfactant, it is particularly excellent in storage stability and can easily suppress an increase in viscosity accompanying an increase in liquid temperature.

[0028] 本発明のフルォロポリマー水性分散液は、例えば、フルォロポリマー粉末、成形体等 に加工することができる。 [0028] The aqueous fluoropolymer dispersion of the present invention can be processed into, for example, a fluoropolymer powder, a molded article and the like.

上記フルォロポリマー粉末は、含フッ素ァ-オン界面活性剤の含有量が非常に低 ヽ ので、優れた成形体の材料として有用である。上記フルォロポリマー粉末は、所望の 用途に応じて、従来の方法により調製することができる。  The fluoropolymer powder has a very low content of the fluorine-containing surfactant, and thus is useful as an excellent molded material. The fluoropolymer powder can be prepared by a conventional method according to the desired use.

[0029] 本発明のフルォロポリマー水性分散液は、そのまま又は各種添加剤を加えて、コー ティング、キャストフィルム、含浸体等にカ卩ェすることができる。 [0029] The aqueous fluoropolymer dispersion of the present invention can be coated on a coating, cast film, impregnated body or the like as it is or with various additives.

上記フルォロポリマー水性分散液は、例えば、オーブン内張り、製氷トレー等の調理 器具、電線、パイプ、船底、高周波プリント基板、搬送用ベルト、アイロン底板におけ る被覆材;繊維基材、織布 ·不織布等を被含浸体とする含浸物;等に加工することが できる。上記繊維基材としては特に限定されず、例えば、ガラス繊維、カーボン繊維、 ァラミド繊維 (ケプラー (登録商標)繊維等)が挙げられる。 The above fluoropolymer aqueous dispersion is, for example, an oven lining, cooking utensils such as ice trays, electric wires, pipes, ship bottoms, high-frequency printed circuit boards, conveyor belts, coating materials on iron bottom plates; fiber base materials, woven fabrics / nonwoven fabrics, etc. Can be processed into an impregnated material, etc. The fiber substrate is not particularly limited. For example, glass fiber, carbon fiber, And aramid fibers (Kepler (registered trademark) fibers, etc.).

上記フルォロポリマー水性分散液の加工は、従来公知の方法にて行うことができる。 発明の効果  Processing of the aqueous fluoropolymer dispersion can be performed by a conventionally known method. The invention's effect

[0030] 本発明のフルォロポリマー水性分散液は、上述の構成よりなるものであるので、含フ ッ素界面活性剤及びフッ素非含有界面活性剤の含有量が極めて低くフルォロポリマ 一が高濃度であっても、分散安定性及び貯蔵安定性に優れており、液温上昇に伴う 粘度上昇を抑制することができる。  [0030] Since the aqueous fluoropolymer dispersion of the present invention has the above-described configuration, the content of the fluorine-containing surfactant and the fluorine-free surfactant is extremely low, and the fluoropolymer mono has a high concentration. Furthermore, it is excellent in dispersion stability and storage stability, and can suppress an increase in viscosity accompanying an increase in liquid temperature.

発明を実施するための最良の形態  BEST MODE FOR CARRYING OUT THE INVENTION

[0031] 本発明を合成例及び試験例により更に詳細に説明するが、本発明はこれらの合成例 及び試験例により限定されるものではない。 [0031] The present invention will be described in more detail with reference to synthesis examples and test examples, but the present invention is not limited to these synthesis examples and test examples.

各合成例及び試験例において、特に説明しない限り、「部」は「質量部」を表す。  In each synthesis example and test example, “part” represents “part by mass” unless otherwise specified.

[0032] 各試験例で行った測定は、以下の方法により行った。 [0032] The measurement performed in each test example was performed by the following method.

(1)平均粒子径  (1) Average particle size

榭脂固形分濃度を 0. 22質量%に調整したフルォロポリマー水性分散液の単位長さ に対する 550nmの投射光の透過率と、透過型電子顕微鏡写真における定方向径を 測定して決定された平均粒径との検量線をもとにして、上記透過率から決定した。 Average particle size determined by measuring the transmittance of 550 nm projection light with respect to the unit length of an aqueous fluoropolymer dispersion adjusted to 0.22% by weight of the solid content of rosin and the directional direction diameter in a transmission electron micrograph Based on the calibration curve with the diameter, it was determined from the transmittance.

(2)フルォロポリマー濃度 (P) (2) Fluoropolymer concentration (P)

試料約 lg (X)を直径 5cmのアルミカップにとり、 100°C、 1時間で乾燥し、更に 300 About lg (X) sample is placed in an aluminum cup with a diameter of 5 cm, dried at 100 ° C for 1 hour, and further 300

。C、 1時間乾燥した加熱残分 (z)に基づき、式: p=zzxx 100 (%)にて決定した。 . C, based on the residue (z) dried for 1 hour, and determined by the formula: p = zzxx 100 (%).

[0033] (3)含フッ素界面活性剤濃度  [0033] (3) Fluorine-containing surfactant concentration

得られた水性分散液に等量のメタノールを添加してソックスレー抽出を行ったのち、 高速液体クロマトグラフィー〔HPLC〕を以下の条件にて行うことにより求めた。なお、 含フッ素界面活性剤濃度算出にあたり、既知の濃度の含フッ素界面活性剤濃度に っ ヽて上記溶出液及び条件にて HPLC測定して得られた検量線を用いた。  The obtained aqueous dispersion was added with an equal amount of methanol and subjected to Soxhlet extraction, and then subjected to high performance liquid chromatography [HPLC] under the following conditions. In calculating the fluorine-containing surfactant concentration, a calibration curve obtained by HPLC measurement with the above-mentioned eluate and conditions was used for a known concentration of the fluorine-containing surfactant.

(測定条件)  (Measurement condition)

カラム; ODS— 120Τ(4. 6 X 250mm,トーソ一社製)  Column; ODS—120 mm (4.6 x 250 mm, manufactured by Toso Co., Ltd.)

展開液;ァセトニトリル ZO. 6質量%過塩素酸水溶液 = 1Z1 (vol/vol%)  Developing solution: acetonitrile ZO. 6 mass% perchloric acid aqueous solution = 1Z1 (vol / vol%)

サンプル量;20 /z L 検出波長; UV210nm Sample volume: 20 / z L Detection wavelength: UV210nm

カラム温度; 40°C  Column temperature; 40 ° C

[0034] (4)フッ素非含有界面活性剤の含有量 (N) [0034] (4) Content of non-fluorine-containing surfactant (N)

試料約 lg (Xg)を直径 5cmのアルミカップにとり、 100°Cにて 1時間で加熱した加熱 残分 (Yg)、更に、得られた加熱残分 (Yg)を 300°Cにて 1時間加熱した加熱残分 (Z 8)ょり、式^= [ ー2) 2] 100 (%)から算出した。  About 1 lg (Xg) of the sample is placed in an aluminum cup with a diameter of 5 cm, and heated residue (Yg) heated at 100 ° C for 1 hour, and the obtained heated residue (Yg) is further heated at 300 ° C for 1 hour. Heated residue (Z 8) was calculated from the equation ^ = [−2) 2] 100 (%).

(5)粘度  (5) Viscosity

B型回転粘度計 (東京計器社製)を用い、 JIS K 6893に準拠して、 25°C又は 35°C における粘度を測定した。  Using a B-type rotational viscometer (manufactured by Tokyo Keiki Co., Ltd.), the viscosity at 25 ° C or 35 ° C was measured in accordance with JIS K 6893.

[0035] (6)機械的安定性 [0035] (6) Mechanical stability

フルォロポリマー水性分散液 50gを、 15000rpmにて 5分間ホモジナイザー CM— 1 00 (ァズワン株式会社製)で高速せん断をかけたのち、 400メッシュのステンレス金網 でろ過して凝集物を回収し、該凝集物を 100°Cにて乾燥して計量した。上記フルォロ ポリマー水性分散液中のフルォロポリマーに対する上記凝集物の百分率を機械的 安定性として求めた。本値が小さいほどフルォロポリマー水性分散液は、せん断に対 して安定であることを示す。  50g of fluoropolymer aqueous dispersion was subjected to high-speed shearing with a homogenizer CM-1 00 (manufactured by Azwan Co., Ltd.) at 15000rpm for 5 minutes, and then filtered through a 400 mesh stainless steel wire mesh to collect the aggregates. Dry and weigh at 100 ° C. The percentage of the aggregate relative to the fluoropolymer in the aqueous fluoropolymer dispersion was determined as mechanical stability. The smaller this value, the more stable the fluoropolymer aqueous dispersion is against shearing.

(7)クラック限界厚み〔CCT〕  (7) Crack limit thickness (CCT)

脱脂したアルミ板(サイズ: 10cm X 15cm)をフルォロポリマー水性分散液 100mlに 浸漬後、 45度の傾斜上で室温にて 5分乾燥し、更に 380°Cで 10分間乾燥したのち、 室温に冷却後、 10倍のルーペでクラック発生の有無を確認する。クラックが発生しな 力つた浸漬済アルミ板のうち、最大の膜厚を膜厚計にて測定し、 CCTとした。  Degreased aluminum plate (size: 10cm x 15cm) is immersed in 100ml of fluoropolymer aqueous dispersion, dried at room temperature on a 45 ° slope for 5 minutes, further dried at 380 ° C for 10 minutes, and then cooled to room temperature Check for cracks with a 10X magnifier. Of the immersed aluminum plates that did not generate cracks, the maximum film thickness was measured with a film thickness meter to obtain CCT.

(8)貯蔵安定性  (8) Storage stability

フルォロポリマー水性分散液 500mlをポリ容器に入れ、 25°C又は 40°Cの恒温室で 2ヶ月間静置した。静置後、緩く攪拌した後にステンレス製 400メッシュでろ過を行い 、メッシュ上に残った凝集分を乾燥し、該凝集分の榭脂固形分に対する割合を 100 分率で表した。貯蔵安定性の悪いものは、多量の凝集分が発生する。  500 ml of an aqueous fluoropolymer dispersion was placed in a plastic container and allowed to stand in a temperature-controlled room at 25 ° C or 40 ° C for 2 months. After standing, the mixture was gently stirred and then filtered through a stainless steel 400 mesh, and the agglomerate remaining on the mesh was dried. Those with poor storage stability generate a large amount of agglomerates.

[0036] 合成例 1 径 6cmのパドル型攪拌機を備えた内容量 5L、径 16cmの円筒型ガラス製容器に、ポ リテトラフルォロエチレン〔PTFE (TFEホモポリマー。以下、同じ。;)〕分散液 (PTFE 含有量 25%、平均粒子径 240nm、パーフルォロオクタン酸アンモ-ゥム〔PFOA〕 含有量: PTFEの 2000ppmに相当する量) 2000gを入れ、 10%アンモニア水溶液 で pHを 9に調整した後、 120rpmの攪拌下にフッ素非含有界面活性剤としてポリオ キシエチレンアルキルエーテル型ノ-オン界面活性剤ノィゲン TDS - 80 (第一工業 製薬社製) 125gを添加し、温水槽中で 40°Cにて均一に混合した。引き続き、攪拌を 行いながら温水槽温度を上げ、内温を 70°Cに到達させたのち、攪拌を停止し、内温 70°Cで 6時間保持した後に、分離した上澄相を除去し、 PTFE水性分散液相を分離 した。 [0036] Synthesis Example 1 Polytetrafluoroethylene [PTFE (TFE homopolymer; the same shall apply hereafter)] dispersion (PTFE content) in a cylindrical glass container with an inner volume of 5 L and a diameter of 16 cm equipped with a paddle type stirrer with a diameter of 6 cm 25%, average particle size 240nm, perfluorooctanoic acid ammonium [PFOA] content: amount equivalent to 2000ppm of PTFE) After adding 2000g and adjusting pH to 9 with 10% aqueous ammonia solution, 120rpm Polyoxyethylene alkyl ether type nonionic surfactant Neugen TDS-80 (Daiichi Kogyo Seiyaku Co., Ltd.) 125g was added as a fluorine-free surfactant under stirring of Mixed. Subsequently, the temperature of the hot water bath was raised while stirring, the internal temperature reached 70 ° C, the stirring was stopped, the internal temperature was maintained at 70 ° C for 6 hours, and then the separated supernatant phase was removed, The PTFE aqueous dispersion phase was separated.

得られた PTFE水性分散液 (濃縮水性分散液)は、 PTFE濃度が 70. 5%、フッ素非 含有界面活性剤含有量が PTFEの 3. 0%に相当する量、 PFOA含有量が PTFEの 48ppmに相当する量であった。  The resulting PTFE aqueous dispersion (concentrated aqueous dispersion) has a PTFE concentration of 70.5%, a fluorine-free surfactant content equivalent to 3.0% of PTFE, and a PFOA content of 48 ppm of PTFE. The amount was equivalent to

この水性分散液に、ノィゲン TDS— 80及びイオン交換水を添カ卩して、 PTFE含有量 60%、フッ素非含有界面活性剤を PTFEの 6. 0%に相当する量になるように調整し た。  Neugen TDS-80 and ion-exchanged water are added to this aqueous dispersion to adjust the PTFE content to 60% and the fluorine-free surfactant to an amount equivalent to 6.0% of PTFE. It was.

[0037] 合成例 2  [0037] Synthesis Example 2

合成例 1にお 、て、 PTFEを変性 PTFE (パーフルォロプロピルビュルエーテル〔PP VE〕変性、変性量 0. 1モル%、平均粒子径 240nm)に変更した以外は、合成例 1と 同様にして、変性 PTFE濃度が 69. 5%、フッ素非含有界面活性剤濃度が 2. 8%、 変性 PFOA量 45ppmの濃縮水性分散液を得た。  The same as Synthesis Example 1 except that PTFE was changed to modified PTFE (perfluoropropyl butyl ether [PP VE] modified, modified amount 0.1 mol%, average particle size 240 nm) in Synthesis Example 1. Thus, a concentrated aqueous dispersion having a modified PTFE concentration of 69.5%, a fluorine-free surfactant concentration of 2.8%, and a modified PFOA amount of 45 ppm was obtained.

この水性分散液に、ノィゲン TDS— 80及びイオン交換水を添カ卩して、変性 PTFE含 有量 60%、フッ素非含有界面活性剤を変性 PTFEの 6. 0%に相当する量になるよう に調整した。  To this aqueous dispersion, Neugen TDS-80 and ion-exchanged water are added so that the modified PTFE content is 60% and the fluorine-free surfactant is equivalent to 6.0% of the modified PTFE. Adjusted.

[0038] 合成例 3 [0038] Synthesis Example 3

合成例 2で得られた濃縮水性分散液にイオン交換水のみを添加して、変性 PTFE含 有量 60%、フッ素非含有界面活性剤濃度が変性 PTFEの 2. 8%に相当する量であ る水性分散液を調製した。 [0039] 合成例 4 Only the ion-exchanged water is added to the concentrated aqueous dispersion obtained in Synthesis Example 2, and the modified PTFE content is 60%, and the concentration of the fluorine-free surfactant is 2.8% of the modified PTFE. An aqueous dispersion was prepared. [0039] Synthesis Example 4

PTFE分散液(i) (PTFE含有量 30%、平均粒子径 220nm、 PFOA含有量: PTFE の 2000ppmに相当する量、フッ素非含有界面活性剤 (製品名: Genapol X080、 クラリアント社製)含有量: PTFEの 5%に相当する量) 2000gを、陰イオン交換榭脂( 製品名:アンバーライト IRA402J、ローム 'アンド'ハース社製) 50mlを充填したカラ ム(直径 2cm)に温度 50°C、空間速度〔SV〕2の条件で通し、 PTFE濃度 30%、フッ 素非含有界面活性剤含有量が PTFEの 4. 9%に相当する量、 PFOA含有量が PT FEの lOppmに相当する量である PTFE分散液 (ii) 1980gを得た。  PTFE dispersion (i) (PTFE content 30%, average particle diameter 220nm, PFOA content: PTFE equivalent to 2000ppm, fluorine-free surfactant (product name: Genapol X080, Clariant) content: An amount equivalent to 5% of PTFE) 2000g, an anion exchange resin (product name: Amberlite IRA402J, manufactured by Rohm 'And' Haas) 50ml in a column (diameter 2cm) filled with a temperature of 50 ° C, space Through the conditions of speed [SV] 2, the PTFE concentration is 30%, the fluorine-free surfactant content is equivalent to 4.9% of PTFE, and the PFOA content is equivalent to lOppm of PTFE. 1980 g of PTFE dispersion (ii) was obtained.

[0040] 上記 PTFE分散液 (ii)に、フッ素非含有界面活性剤 (製品名: Genapol X080、クラ リアント社製) 60gを添加し、温水槽中で 40°Cにて均一に混合した。引き続き、攪拌 を行いながら温水槽温度を上げ、内温を 60°Cに到達させた後、攪拌を停止し内温を 60°Cに 4時間保持して、分離した上澄相を除去し、 PTFE水性分散液相を分離した 上記 PTFE水性分散液は、 PTFE濃度が 69. 8%、フッ素非含有界面活性剤含有量 力 SpTFEの 2. 5%に相当する量、 PFOA含有量が PTFEの 2ppmに相当する量であ つた o [0040] 60 g of a fluorine-free surfactant (product name: Genapol X080, manufactured by Clariant) was added to the PTFE dispersion (ii) and mixed uniformly at 40 ° C in a hot water bath. Subsequently, the temperature of the hot water bath was raised while stirring, and the internal temperature reached 60 ° C. Then, stirring was stopped and the internal temperature was maintained at 60 ° C for 4 hours to remove the separated supernatant phase. The PTFE aqueous dispersion separated from the PTFE aqueous dispersion phase has a PTFE concentration of 69.8%, a fluorine-free surfactant content, an amount equivalent to 2.5% of SpTFE, and a PFOA content of 2 ppm of PTFE. Is equivalent to o

これにイオン交換水及び Genapol X080を添加して、 PTFE60%、フッ素非含有界 面活性剤を PTFEの 6%に相当する量に調整した。  Ion exchange water and Genapol X080 were added to this to adjust the amount of PTFE 60% and fluorine-free surfactant to 6% of PTFE.

[0041] 合成例 5 [0041] Synthesis Example 5

PTFEを変性 PTFE (HFPで 0. 05モル%変性、平均粒子径 220nm)に変更した以 外は、合成例 4と同様にして、イオン交換処理及び濃縮を行い、変性 PTFE濃度が 7 0. 5%、フッ素非含有界面活性剤含有量が変性 PTFEの 2. 5%に相当する量、 PF OA含有量が変性 PTFEの 2ppmに相当する量である変性 PTFEの水性分散液を得 た。  Except for changing PTFE to modified PTFE (0.05 mol% modified with HFP, average particle size 220 nm), ion exchange treatment and concentration were performed in the same manner as in Synthesis Example 4 to obtain a modified PTFE concentration of 70.5. %, A fluorine-free surfactant content corresponding to 2.5% of the modified PTFE, and a PFOA content corresponding to 2 ppm of the modified PTFE were obtained.

これにイオン交換水及び上記フッ素非含有界面活性剤を添加して、変性 PTFE60 %、フッ素非含有界面活性剤含有量を変性 PTFEの 6%に相当する量に調整した。  Ion exchange water and the above-mentioned non-fluorine-containing surfactant were added thereto, and the modified PTFE 60% and the content of non-fluorine-containing surfactant were adjusted to an amount corresponding to 6% of the modified PTFE.

[0042] 合成例 6 [0042] Synthesis Example 6

変性 PTFE60%、フッ素非含有界面活性剤濃度が 4. 8%となるよう、フッ素非含有 界面活性剤と水とを加える以外は、合成例 5と同様にフルォロポリマー水性分散液を 調製した。 Modified PTFE 60%, fluorine-free surfactant so that the concentration of surfactant containing no fluorine is 4.8% A fluoropolymer aqueous dispersion was prepared in the same manner as in Synthesis Example 5 except that the surfactant and water were added.

[0043] 合成例 7 [0043] Synthesis Example 7

合成例 6のフルォロポリマー水性分散液に、更に、アルキルスルホン酸 Na塩〔SAS〕 In addition to the aqueous fluoropolymer dispersion of Synthesis Example 6, the alkylsulfonic acid Na salt [SAS]

(クラリアント社製)を変性 PTFEの lOOOppmに相当する量となるように添加した。 (Manufactured by Clariant) was added in an amount corresponding to lOOOOppm of the modified PTFE.

[0044] 実施例及び比較例 [0044] Examples and Comparative Examples

各合成例の水性分散液について、粘度、機械的安定性、クラック限界厚み〔CCT〕 及び貯蔵安定性を測定した。  Viscosity, mechanical stability, crack limit thickness [CCT] and storage stability were measured for the aqueous dispersions of each synthesis example.

各測定結果を表 1に示す。  Table 1 shows the measurement results.

[0045] [表 1] [0045] [Table 1]

Figure imgf000015_0001
Figure imgf000015_0001

[0046] 表 1中、各界面活性剤の含有量はフルォロポリマーに対する割合で表している。 各結果を比較したところ、各実施例の水性分散液は、いずれも貯蔵安定性に優れ、 液温上昇に伴う粘度上昇を抑制することができたが、比較例の水性分散液は、液温 上昇に伴い粘度が著しく上昇し、特に 40°Cにおける貯蔵安定性に劣っていた。 産業上の利用可能性 [0046] In Table 1, the content of each surfactant is expressed as a ratio to the fluoropolymer. When the results were compared, all of the aqueous dispersions of each example were excellent in storage stability and could suppress an increase in viscosity accompanying an increase in the liquid temperature. The viscosity increased remarkably with the increase, and in particular, the storage stability at 40 ° C was inferior. Industrial applicability

[0047] 本発明のフルォロポリマー水性分散液は、上述の構成よりなるものであるので、含フ ッ素界面活性剤及びフッ素非含有界面活性剤の含有量が極めて低くフルォロポリマ 一が高濃度であっても、分散安定性及び貯蔵安定性に優れており、液温上昇に伴う 粘度上昇を抑制することができる。 [0047] Since the aqueous fluoropolymer dispersion of the present invention has the above-described configuration, the content of the fluorine-containing surfactant and the fluorine-free surfactant is extremely low, and the fluoropolymer mono has a high concentration. Furthermore, it is excellent in dispersion stability and storage stability, and can suppress an increase in viscosity accompanying an increase in liquid temperature.

Claims

請求の範囲 The scope of the claims [1] フッ素非含有界面活性剤の存在下に水性媒体中にフルォロポリマーからなる粒子が 分散して!/、るフルォロポリマー水性分散液であって、  [1] A fluoropolymer aqueous dispersion in which particles made of a fluoropolymer are dispersed in an aqueous medium in the presence of a fluorine-free surfactant. 前記フルォロポリマーからなる粒子は、前記フルォロポリマー水性分散液の 35〜70 質量%であり、  The particles made of the fluoropolymer are 35 to 70% by mass of the aqueous fluoropolymer dispersion, 前記フルォロポリマー水性分散液中における含フッ素界面活性剤は、前記フルォロ ポリマーの固形分の 50ppmに相当する量以下であり、  The fluorine-containing surfactant in the aqueous fluoropolymer dispersion is below the amount corresponding to 50 ppm of the solid content of the fluoropolymer, 前記フッ素非含有界面活性剤は、前記フルォロポリマーの固形分の 1質量%以上、 5質量%以下に相当する量であり、  The fluorine-free surfactant is an amount corresponding to 1% by mass or more and 5% by mass or less of the solid content of the fluoropolymer, 前記フルォロポリマーは、変性ポリテトラフルォロエチレンである  The fluoropolymer is a modified polytetrafluoroethylene ことを特徴とするフルォロポリマー水性分散液。  An aqueous fluoropolymer dispersion characterized by the above. [2] フッ素非含有界面活性剤は、フルォロポリマー力もなる粒子の 1〜3. 5質量%に相 当する量である請求項 1記載のフルォロポリマー水性分散液。 [2] The aqueous fluoropolymer dispersion according to claim 1, wherein the fluorine-free surfactant is in an amount corresponding to 1 to 3.5% by mass of the particles having a fluoropolymer power. [3] フッ素非含有界面活性剤は、フッ素非含有ノ-オン界面活性剤である請求項 1又は[3] The fluorine-free surfactant is a fluorine-free non-ionic surfactant, or 2記載のフルォロポリマー水性分散液。 2. The aqueous fluoropolymer dispersion according to 2. [4] フッ素非含有界面活性剤は、疎水基にベンゼン環を有さな 、フッ素非含有化合物か らなるものである請求項 1〜3の何れか 1項に記載のフルォロポリマー水性分散液。 [4] The fluoropolymer aqueous dispersion according to any one of [1] to [3], wherein the non-fluorine-containing surfactant comprises a non-fluorine-containing compound having no hydrophobic group and a benzene ring. [5] 含フッ素界面活性剤は、分子量が 1000以下である含フッ素化合物からなるものであ る請求項 1〜4の何れか 1項に記載のフルォロポリマー水性分散液。 [5] The aqueous fluoropolymer dispersion according to any one of claims 1 to 4, wherein the fluorine-containing surfactant comprises a fluorine-containing compound having a molecular weight of 1000 or less. [6] 含フッ素界面活性剤は、炭素数が 5〜12である含フッ素化合物からなるものである請 求項 1〜5の何れ力 1項に記載のフルォロポリマー水性分散液。 [6] The aqueous fluoropolymer dispersion according to any one of claims 1 to 5, wherein the fluorine-containing surfactant is composed of a fluorine-containing compound having 5 to 12 carbon atoms. [7] 含フッ素界面活性剤は、パーフルォロカルボン酸又はその塩力もなるものである請求 項 1〜6の何れ力 1項に記載のフルォロポリマー水性分散液。 7. The aqueous fluoropolymer dispersion according to any one of claims 1 to 6, wherein the fluorine-containing surfactant also has perfluorocarboxylic acid or a salt power thereof.
PCT/JP2006/326246 2005-12-28 2006-12-28 Aqueous fluoropolymer dispersion Ceased WO2007074901A1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2007521728A JP4985399B2 (en) 2005-12-28 2006-12-28 Fluoropolymer aqueous dispersion

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP2005380423 2005-12-28
JP2005-380423 2005-12-28

Publications (1)

Publication Number Publication Date
WO2007074901A1 true WO2007074901A1 (en) 2007-07-05

Family

ID=38218122

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/JP2006/326246 Ceased WO2007074901A1 (en) 2005-12-28 2006-12-28 Aqueous fluoropolymer dispersion

Country Status (2)

Country Link
JP (1) JP4985399B2 (en)
WO (1) WO2007074901A1 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2008032613A1 (en) * 2006-09-11 2008-03-20 Asahi Glass Company, Limited Process for producing melt-moldable tetrafluoroethylene copolymer
WO2019235439A1 (en) * 2018-06-06 2019-12-12 Agc株式会社 Liquid dispersion, production method for resin-including metal foil, and production method for printed board

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002532583A (en) * 1998-12-11 2002-10-02 ダイネオン・ゲゼルシャフト・ミト・ベシュレンクテル・ハフツング・ウント・コンパニー・コマンディトゲゼルシャフト Aqueous dispersion of fluoropolymer
WO2004050719A1 (en) * 2002-11-29 2004-06-17 Daikin Industries, Ltd. Method for purification of aqueous fluoropolymer emulsions, purified emulsions, and fluorine-containing finished articles
JP2005501956A (en) * 2001-09-05 2005-01-20 スリーエム イノベイティブ プロパティズ カンパニー Fluoropolymer dispersion with little or no low molecular weight fluorinated surfactant
JP2006523758A (en) * 2003-02-28 2006-10-19 スリーエム イノベイティブ プロパティズ カンパニー Fluoropolymer dispersions with or without low molecular weight fluorinated surfactants

Family Cites Families (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6956078B2 (en) * 2002-01-04 2005-10-18 E.I. Du Pont De Nemours And Company Concentrated fluoropolymer dispersions
JP4206714B2 (en) * 2002-09-10 2009-01-14 ダイキン工業株式会社 Fluororesin aqueous dispersion, fluororesin aqueous composition, coating and film
JPWO2005056614A1 (en) * 2003-12-09 2007-07-05 ダイキン工業株式会社 Fluoropolymer aqueous dispersion and process for producing the same
JPWO2006035726A1 (en) * 2004-09-27 2008-05-15 ダイキン工業株式会社 Polytetrafluoroethylene aqueous dispersion composition, polytetrafluoroethylene resin film, and polytetrafluoroethylene resin impregnated body
JP2006104391A (en) * 2004-10-07 2006-04-20 Daikin Ind Ltd Method for producing aqueous fluoropolymer dispersion
US20060183842A1 (en) * 2005-02-10 2006-08-17 Johnson David W Fluoropolymer dispersions with reduced fluorosurfactant content and high shear stability
JP2006316242A (en) * 2005-04-13 2006-11-24 Daikin Ind Ltd Method for producing aqueous fluoropolymer dispersion
US7612139B2 (en) * 2005-05-20 2009-11-03 E.I. Du Pont De Nemours And Company Core/shell fluoropolymer dispersions with low fluorosurfactant content
CN101184791B (en) * 2005-06-24 2011-04-13 大金工业株式会社 Aqueous fluorine-containing polymer dispersion and method for production thereof
JP2009057392A (en) * 2005-12-28 2009-03-19 Daikin Ind Ltd Fluoropolymer aqueous dispersion
JP2007177188A (en) * 2005-12-28 2007-07-12 Daikin Ind Ltd Fluoropolymer aqueous dispersion and process for producing the same
JP2007197721A (en) * 2005-12-28 2007-08-09 Daikin Ind Ltd Fluoropolymer aqueous dispersion

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002532583A (en) * 1998-12-11 2002-10-02 ダイネオン・ゲゼルシャフト・ミト・ベシュレンクテル・ハフツング・ウント・コンパニー・コマンディトゲゼルシャフト Aqueous dispersion of fluoropolymer
JP2005501956A (en) * 2001-09-05 2005-01-20 スリーエム イノベイティブ プロパティズ カンパニー Fluoropolymer dispersion with little or no low molecular weight fluorinated surfactant
WO2004050719A1 (en) * 2002-11-29 2004-06-17 Daikin Industries, Ltd. Method for purification of aqueous fluoropolymer emulsions, purified emulsions, and fluorine-containing finished articles
JP2006523758A (en) * 2003-02-28 2006-10-19 スリーエム イノベイティブ プロパティズ カンパニー Fluoropolymer dispersions with or without low molecular weight fluorinated surfactants

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2008032613A1 (en) * 2006-09-11 2008-03-20 Asahi Glass Company, Limited Process for producing melt-moldable tetrafluoroethylene copolymer
US8470942B2 (en) 2006-09-11 2013-06-25 Asahi Glass Company, Limited Method for producing melt-moldable tetrafluoroethylene copolymer
WO2019235439A1 (en) * 2018-06-06 2019-12-12 Agc株式会社 Liquid dispersion, production method for resin-including metal foil, and production method for printed board
CN112236473A (en) * 2018-06-06 2021-01-15 Agc株式会社 Dispersion, method for producing metal foil with resin, and method for producing printed circuit board
KR20210018190A (en) * 2018-06-06 2021-02-17 에이지씨 가부시키가이샤 Dispersion, method for manufacturing metal foil with resin, and method for manufacturing printed board
KR102708267B1 (en) 2018-06-06 2024-09-20 에이지씨 가부시키가이샤 Method for producing a dispersion, a metal foil with a resin attached thereto, and a method for producing a printed circuit board

Also Published As

Publication number Publication date
JPWO2007074901A1 (en) 2009-06-04
JP4985399B2 (en) 2012-07-25

Similar Documents

Publication Publication Date Title
CN103443196B (en) Aqueous fluorine-containing polymer dispersion
JP6746608B2 (en) Polytetrafluoroethylene aqueous dispersion
JP5435089B2 (en) Fluorine-containing polymer aqueous dispersion
JP2007511657A (en) Aqueous dispersion of polytetrafluoroethylene with a small amount of fluorinated surfactant
CN104812780A (en) PTFE aqueous dispersion and PTFE fine powder
JP5332788B2 (en) Fluorine-containing polymer aqueous dispersion
US20110144255A1 (en) Aqueous fluoropolymer dispersion
JP5417847B2 (en) Method for producing fluoropolymer aqueous dispersion and fluoropolymer aqueous dispersion
JP4798132B2 (en) Fluorine-containing polymer aqueous dispersion and method for producing the same
JP5195425B2 (en) Fluororesin aqueous dispersion and method for producing the same
WO2007074901A1 (en) Aqueous fluoropolymer dispersion
JP5251013B2 (en) Method for producing fluororesin aqueous dispersion
WO2007074902A1 (en) Aqueous fluoropolymer dispersion
CN101155858A (en) Process for producing aqueous fluoropolymer dispersion
JP2007177188A (en) Fluoropolymer aqueous dispersion and process for producing the same
JP2007197721A (en) Fluoropolymer aqueous dispersion
JP2008214400A (en) Method for producing fluororesin aqueous dispersion
JPWO2006077737A1 (en) Fluorine-containing polymer aqueous dispersion production method

Legal Events

Date Code Title Description
WWE Wipo information: entry into national phase

Ref document number: 2007521728

Country of ref document: JP

121 Ep: the epo has been informed by wipo that ep was designated in this application
NENP Non-entry into the national phase

Ref country code: DE

122 Ep: pct application non-entry in european phase

Ref document number: 06843624

Country of ref document: EP

Kind code of ref document: A1