Fluoropolymer compositions and methods of making

Abstract

A composition having reduced haze is disclosed, comprising a PVDF copolymer, 0.005-5% of one or more inorganic or polymeric nucleating additives, and 0.01-20% of one or more dispersing agents, wherein at least one comonomer is selected from hexafluoropropene, 2,3,3,3-tetrafluoropropylene, and 3,3,3-trifluoropropene. A method for preparing the composition is also disclosed.

Description

[Technical Field]

[0001] The present invention provides compositions and methods that allow for the fine dispersion of inorganic or polymeric nucleating additives in fluorinated copolymers. [Background technology]

[0002] PVDF homopolymer has a high degree of crystallinity, which allows for excellent physical properties. For some applications, PVDF is copolymerized with other fluorinated comonomers to create PVDF copolymers. Comonomers such as hexafluoropropene, 2,3,3,3-tetrafluoropropene, and 3,3,3-trifluoropropene tend to lower the melting point of PVDF and slow its crystallization rate. This results in material parts with inconsistent physical properties, such as optical haze. Summary of the Invention [Problem to be solved by the invention]

[0003] The present invention provides a method for increasing the crystallization rate of PVDF copolymers using inorganic or polymeric nucleating additives. Several inorganic and polymeric nucleating additives have been described for polyolefins and PVDF homopolymers. It has been found that selected nucleating additives, such as carbon black and PTFE polymers, can be used efficiently in PVDF copolymers, resulting in reduced haze in parts made with the copolymers. Furthermore, the present invention provides the use of a dispersing agent to facilitate dispersion of the nucleating additive in the copolymer. Because PVDF copolymers are more hydrophobic than PVDF homopolymers, dispersion of the nucleating additive presents a challenge. Insufficient dispersion of the nucleating additive can result in high optical haze due to the size of the nucleating additive itself in the final material. The dispersing agent allows the nucleating additive to be present in the composition as small particles (discrete domains in the copolymer matrix), with more than 50%, preferably more than 70%, and most preferably more than 90% of the particles having a size of less than 5 μm, preferably less than 2 μm, and most preferably less than 1 μm. The present invention also provides a method for producing a composition having a low optical haze of less than 30%, preferably less than 20%, as measured by ASTM D1003 on a 1 mm part compression molded using the composition. [Means for solving the problem]

[0004] Aspects of the present invention: Aspect 1: A composition comprising: a. PVDF copolymers, wherein at least one comonomer is selected from hexafluoropropene, 2,3,3,3-tetrafluoropropylene, 3,3,3-trifluoropropene, and wherein VDF constitutes more than 60% of all monomers, preferably more than 70% of all monomers; and b. 0.005 to 5% of one or more inorganic or polymeric nucleating additives; and c. 0.1 to 20% of one or more dispersants Including, The composition, wherein a 1 mm thick part produced by compression molding at 230°C has an optical haze according to ASTM D1003 of less than 40%.

[0005] Aspect 2: The composition of aspect 1, wherein the dispersant is present at 1-15%.

[0006] Aspect 3: The composition of aspect 1 or 2, wherein the nucleating additive is present as particles, and greater than 50%, preferably greater than 70%, and most preferably greater than 90% of the particles have a size less than 5 μm, preferably less than 2 μm, and most preferably less than 1 μm.

[0007] Aspect 4: The composition of aspect 1 or 2, wherein the nucleating additive has an average particle size of less than 2 μm, and most preferably less than 1 μm.

[0008] Aspect 5: The composition of any one of Aspects 1 to 4, wherein the nucleating additive is selected from the group consisting of inorganic particles, organic dyes, benzene derivatives, fluorinated polymers, crosslinked polymer particles, and combinations thereof.

[0009] Aspect 6: The composition of aspect 5, wherein the inorganic particles are selected from carbon black, activated carbon, silica, clay, aluminosilicates, talc, mica, calcium carbonate, titania, and combinations thereof.

[0010] Aspect 7: The composition of aspect 5, wherein the organic dye is selected from flavanthrones, idanthrones, perienes, quinophthalones, phthalocyanines, and combinations thereof.

[0011] Aspect 8: The composition of aspect 5, wherein the fluorinated polymer is chosen from polytetrafluoroethylene polymers and copolymers.

[0012] Aspect 9: The composition of aspect 5, wherein the crosslinked polymer particles are selected from polymers made by suspension or emulsion polymerization in the presence of a crosslinking monomer.

[0013] Aspect 10: The composition of any one of Aspects 1-9, wherein the dispersing agent is chosen from one or more plasticizers.

[0014] Aspect 11: The composition of aspect 10, wherein the plasticizer is selected from the group consisting of acrylic, styrene, polyester, and combinations thereof.

[0015] Aspect 12: The composition of aspect 11, wherein the acrylic polymer is chosen from poly(methyl methacrylate) oligomers, polymers, and copolymers.

[0016] Aspect 13: The composition of aspect 11, wherein the polyester is selected from the group consisting of polyethylene glycol, polypropylene glycol, and blends thereof.

[0017] Embodiment 14: A method of preparing the composition of any of embodiments 1-13, comprising: d. Mixing the nucleating additive with the dispersing agent in a mixer or extruder e. Mixing the blend of (d) with a VDF-based copolymer in an extruder. A method comprising:

[0018] Embodiment 15: A method of preparing the composition of any of embodiments 1-13, comprising: f. Mixing the VDF-based copolymer latex with a nucleating additive and / or a dispersant. g. Drying the latex into a solid material A method comprising:

[0019] Embodiment 16: An article comprising the composition of any of embodiments 1-13, wherein the article can be a film, a sheet, a rod, a multilayer part, or any other shape or configuration.

[0020] Embodiment 17: The article of embodiment 16, wherein the article is a melt-processed article.

[0021] Aspect 18: Use of the article according to aspect 17 for wire and cable, oil and gas, consumer electronics, photovoltaic cells, protective films, packaging, medical devices. [Brief explanation of the drawings]

[0022] [Figure 1] Optical image (Nikon ME600 optical microscope) of a part made in Comparative Example 1. [Figure 2] Optical image (Nikon ME600 optical microscope) of the part fabricated in Example 1. DETAILED DESCRIPTION OF THE INVENTION

[0023] The references cited in this application are hereby incorporated by reference.

[0024] Percentages used herein are weight percent unless otherwise specified, and molecular weights are weight average molecular weight unless otherwise specified.

[0025] "Copolymer" is used to mean a polymer having two or more different monomer units. "Polymer" is used to mean both homopolymers and copolymers. For example, as used herein, "PVDF" and "polyvinylidene fluoride" are used to imply both homopolymers and copolymers unless otherwise specified. Polymers can be linear, branched, star, comb, block, crosslinked, or other structures. Polymers can be homogeneous, heterogeneous, or have a gradient distribution of comonomer units. As used herein, unless otherwise specified, percent means weight percent. Molecular weight is the weight average molecular weight as measured by gas permeation chromatography (GPC). An alternative to GPC for quantifying molecular weight is melt flow rate (MFR). Higher molecular weights (MW) have lower MFRs or melt viscosities (MV) measured at 230°C and 100 s-1, and higher MW resins have higher MVs. For PVDF polymers, extrusion grades typically have a MV of 12-40 kpoise at 232°C and 100 sec-1. Injection grades have a MV of 1-11 kpoise.

[0026] The particle size of the polymer powder can be measured using a Malvern Masturizer 2000 particle size analyzer. The data is reported as volume average particle size (diameter).

[0027] Powder / latex average discrete particle size is measured using a NICOMP™ 380 submicron particle sizer. Data is reported as volume average particle size (diameter). Discrete means that the particles are not agglomerated.

[0028] PVDF copolymer The term PVDF copolymer refers to a copolymer of vinylidene fluoride (VDF) with one or more other fluorinated comonomers. The PVDF copolymer of the present invention comprises vinylidene fluoride units at more than 50% of the total weight of all monomer units in the polymer, more preferably at more than 60% of the total weight of units, and most preferably at more than 70% of the total weight of units. The fluorinated comonomer comprises at least 0.5% by weight, preferably at least 1% by weight, and more preferably at least 4% by weight of the PVDF copolymer. The fluorinated comonomer is 0.5% to 30% by weight, preferably 1% to 20% by weight.

[0029] The fluorinated comonomer is selected from compounds containing a vinyl group that can be opened to polymerize and directly bonded to this vinyl group contains at least one fluorine atom, at least one fluoroalkyl group, or at least one fluoroalkoxy group, excluding VDF, which is already present in the PVDF copolymer. Examples of fluorinated comonomers include, but are not limited to: vinyl fluoride; trifluoroethylene (VF3); chlorotrifluoroethylene (CTFE); 1,2-difluoroethylene; tetrafluoroethylene (TFE); hexafluoropropylene (HFP); 2,3,3,3-tetrafluoropropylene; 1,3,3,3-tetrafluoropropylene; 3,3,3-trifluoropropylene; perfluoro(alkyl vinyl) ethers such as perfluoro(methyl vinyl) ether (PMVE), perfluoro(ethyl vinyl) ether (PEVE) and perfluoro(propyl vinyl) ether (PPVE); perfluoro(1,3-dioxole); perfluoro(2,2-dimethyl-1,3-dioxole) (PDD). Preferred PVDF copolymers include copolymers of VDF and HFP, copolymers of VDF and 2,3,3,3-tetrafluoropropylene, copolymers of VDF and 3,3,3-trifluoropropylene, and terpolymers of VDF, HFP, and TFE (THV).

[0030] The PVDF copolymer may be a copolymer of VDF and HFP. In one embodiment, the PVDF copolymer contains at least 1% to 30% by weight, preferably at most 25% by weight, more preferably at most 15% by weight, of hexafluoropropene (HFP) units, and at least 70% by weight, preferably at least 75% by weight, more preferably at least 85% by weight or more of VDF units.

[0031] The PVDF copolymers for use in the present invention have a high molecular weight. As used herein, high molecular weight refers to a PVDF copolymer that can be sintered at 450°F for 100 seconds according to ASTM method D-3835. -1 By "melt viscosity" we mean a melt viscosity of greater than 1.0 kpoise, preferably greater than 5 kpoise, as measured by .mu.m.

[0032] The PVDF copolymers used in this invention are generally prepared by means known in the art using aqueous free-radical emulsion polymerization. However, suspension, solution, and supercritical CO2 polymerization processes can also be used. In a typical emulsion polymerization process, a reactor is charged with deionized water, a water-soluble surfactant capable of emulsifying the reactant mass during polymerization, and an optional paraffin wax antifouling agent. The mixture is stirred and deoxygenated. A predetermined amount of chain transfer agent, CTA, is then introduced into the reactor, the reactor temperature is raised to the desired level, and vinylidene fluoride and one or more comonomers are fed into the reactor. Once the initial charge of vinylidene fluoride and comonomers has been introduced and the pressure in the reactor has reached the desired level, an initiator emulsion or solution is introduced to initiate the polymerization reaction. The reaction temperature can vary depending on the characteristics of the initiator used, and is known to those skilled in the art. Typically, the temperature is between about 30°C and 150°C, preferably between about 60°C and 120°C. Once the desired amount of polymer is reached in the reactor, the monomer feed is stopped, but the initiator feed is optionally continued to consume the residual monomer. The residual gas (including unreacted monomer) is vented, and the latex is recovered from the reactor.

[0033] The surfactant used in the polymerization can be any surfactant known in the art to be useful in PVDF emulsion polymerization, including perfluorinated, partially fluorinated, and non-fluorinated surfactants. Preferably, the PVDF copolymer emulsion of the present invention is fluorinated surfactant-free, and no fluorinated surfactants are used in any part of the polymerization. Non-fluorinated surfactants useful in PVDF polymerization can be both ionic and non-ionic in nature, and include, but are not limited to, 3-allyloxy-2-hydroxy-1-propanesulfonate, polyvinylphosphonic acid, polyacrylic acid, polyvinylsulfonic acid, and salts thereof, polyethylene glycol and / or polypropylene glycol and their block copolymers, alkylphosphonates, and siloxane-based surfactants. In one embodiment, the emulsion polymerization is surfactant-free.

[0034] PVDF copolymerization generally results in a latex having a solids level of 10-60% by weight, preferably 10-50%, and a latex volume average particle size of less than 500 nm, preferably less than 400 nm, more preferably less than 300 nm. The discrete volume average particle size is generally at least 20 nm, preferably at least 50 nm.

[0035] Small amounts (preferably less than 10% by weight, preferably less than 5% by weight) of one or more other water-miscible solvents, such as ethylene glycol, may be mixed into the PVDF latex to improve freeze-thaw stability.

[0036] The PVDF copolymer latex can be used in the process of the present invention as a latex, or it can be first dried to a powder by means known in the art, such as, but not limited to, spray drying, freeze drying, coagulation, and drum drying. The dried PVDF copolymer powder has a volume average particle size of 0.5 to 200 μm, preferably 1 to 100 μm, more preferably 2 to 50 μm, and most preferably 3 to 20 μm.

[0037] In one embodiment, copolymers of VDF and HFP are used. Particularly useful copolymers include, but are not limited to, KYNAR™ resins from Arkema Inc., especially KYNAR 2500, KYNAR 2750, KYNAR 2800, and KYNAR 2850.

[0038] PVDF / HFP copolymers have lower melting points, lower crystallinity, and slower crystallization rates than PVDF homopolymers, the latter of which is particularly problematic when producing materials with low optical haze, as the optical haze becomes highly dependent on the melting and cooling processes used to produce plastic parts from the copolymer.

[0039] The haze value can be reduced by more than 10%, preferably more than 20%, and even more preferably more than 40% for a composition that includes a dispersant and a nucleating agent compared to the same composition without the dispersant and the nucleating agent.

[0040] For example, copolymers of VDF and HFP containing up to 22% by weight of HFP can be compression molded, injection molded, or extruded into 1 mm parts with high haze of over 40%. Generally, slow cooling rates, typical of compression molding, produce parts with high haze. The compositions of the present invention can be processed into 1 mm parts with low haze of 40% or less.

[0041] In one variant of the invention, the PVDF copolymer is a functionalized PVDF copolymer, such as maleic anhydride grafted. The functionality improves the compatibility of the polymer with the additives of the invention.

[0042] Nucleating Additives The nucleating additive is selected from inorganic or polymeric materials.

[0043] There may be one or more nucleating additives. The total amount of nucleating additives in the present invention is at least 0.005% by weight and no more than 15% by weight, based on the total composition.

[0044] The amount of any one nucleating additive may be 0.005 to 10% by weight, preferably 0.05 to 5% by weight, more preferably 0.09 to 3.5% by weight, based on the total composition.

[0045] Examples of nucleating additives include, but are not limited to, inorganic particles, organic dyes, benzene derivatives, perfluorinated polymers, crosslinked polymer particles.

[0046] Examples of inorganic nucleating additives include, but are not limited to, carbon black, activated carbon, silica, clay, aluminosilicate, talc, mica, calcium carbonate, and titania. Examples of organic dye nucleating additives include, but are not limited to, flavanthrones, idanthrones, perylenes, quinophthalones, and phthalocyanines. Examples of fluorinated polymers include, but are not limited to, polytetrafluoroethylene polymers and copolymers. An example of a fluorinated polymer nucleating additive is perfluorinated polytetrafluoroethylene (PTFE). Examples of crosslinked polymer particle nucleating additives include, but are not limited to, polymers prepared by suspension or emulsion polymerization in the presence of crosslinking monomers.

[0047] Dispersants The amount of dispersant used in the present invention is 0.1 to 20%, preferably 1 to 15%, more preferably 2 to 10% of one or more dispersants based on the total composition.

[0048] The dispersant may be one or more plasticizers. Examples of dispersants include acrylics, styrenes, and polyesters. Acrylics include, but are not limited to, poly(methyl methacrylate) oligomers, polymers, and copolymers. Polyesters include, but are not limited to, polyethylene glycol and polypropylene glycol. Acrylics and polyesters are preferred.

[0049] Mixing Process The PVDF copolymer, dispersant, and nucleating additive can be mixed in an aqueous medium and then dried into a particulate material, or they can be mixed as solid materials. The dispersant can be mixed with the PVDF copolymer and nucleating additive in one step, first with the nucleating additive and then with the PVDF copolymer, or first with the PVDF copolymer and then with the nucleating additive. Any mixing equipment known in the art can be utilized, including static mixers, Brabenders, and extruders.

[0050] In one embodiment, an intimate blend of a PVDF copolymer, a nucleating additive, and a dispersing agent can be prepared by co-spray drying the components mixed in an aqueous medium. Effective amounts of a PVDF copolymer latex can be mixed with a nucleating additive (latex, solution, or solid form) and a dispersing agent (latex, solution, or solid form) and then co-sprayed to achieve a nanoscale, well-mixed dry powder. This co-spray-dried composite can then be processed into the desired shape by any melt process known in the art, such as compression molding, injection molding, extrusion, or co-extrusion. The use of a PVDF latex with a small particle size (typically 20-400 nm) to create the blends of the present invention results in a very intimate blend, allowing for excellent dispersion of the nucleating additive in the material and further contributing to reduced optical haze.

[0051] use The advantageous properties of PVDF copolymers, including chemical inertness, biological purity, and excellent mechanical and thermomechanical properties, combined with consistent low haze, allow the compositions of the present invention to be used in many applications.

[0052] The compositions of the present invention are melt processed to produce articles. The articles of the present invention are melt processed articles.

[0053] Some articles made with the compositions of the present invention include, but are not limited to, films, sheets, rods, and multilayer parts. Applications may include wire and cable, oil and gas, consumer electronics, photovoltaic cells, protective films, packaging, and medical devices. [Example]

[0054] Comparative Example 1 VDF / HFP (15 wt% HFP) copolymer was combined with a nucleating additive, carbon black, with a discrete particle size of 20 nm (0.05 wt% of the blend) in a twin-screw extruder at 230 °C to produce pellets. The pellets were compression molded into 1 mm thick plaques at 230 °C under 5 MT pressure and cooled to room temperature over 10 minutes. A 1 mm control plaque of pure VDF / HFP copolymer was also compression molded under the same conditions. ASTM D1003 was used to measure the haze of the sample plaques. The haze of the pure copolymer was 72%, while the haze of the copolymer / carbon black blend was 65%. The reduction in haze with the addition of carbon black indicates that it functions as a nucleating additive, generating small alpha crystals that do not diffract light well. However, the reduction in haze is limited by poor dispersion of the 20 nm carbon black particles, which are present in the final material as agglomerates larger than 1 μm. In fact, optical microscopy shows that more than 70% of carbon black particles exist in the form of aggregates larger than 2 μm (Figure 1).

[0055] Example 1 Plexiglas V825-100, an acrylic polymer manufactured by Arkema, was first mixed with 0.5 wt.% carbon black with a 20 nm discrete particle size in a high-shear mixer (dry blend). The resulting material was then blended at 10 wt.% with a VDF / HFP (15 wt.% HFP) copolymer (dry) in a twin-screw extruder at 230°C to produce pellets. The final material contained 9.95 wt.% VDF / HFP polymer, dispersant V825-100, and 0.05 wt.% nucleating additive carbon black. The pellets were compression molded into 1 mm thick plaques at 230°C under 5 MT pressure and cooled to room temperature over 10 minutes. ASTM D1003 was used to measure the haze of the sample plaques. The haze was 35%. This was significantly lower than that obtained in Comparative Example 1, demonstrating the effectiveness of the dispersant. In fact, optical microscopy shows carbon black particles less than 2 μm in size, with less than 30% of the carbon black present in the form of aggregates greater than 2 μm (Figure 2).

[0056] Example 2 An acrylic copolymer, Paraloid B-44, manufactured by Dow, was first mixed with 0.5 wt.% carbon black with a 20 nm discrete particle size in a high-shear mixer (dry blend). The resulting material was then blended at 10 wt.% with a VDF / HFP (15 wt.% HFP) copolymer (dry) in a twin-screw extruder at 230°C to produce pellets. The final blended material contained VDF / HFP polymer, 9.95 wt.% dispersant B-44, and 0.05 wt.% nucleating additive carbon black. The pellets were compression molded into 1 mm thick plaques at 230°C under a pressure of 5 MT and cooled to room temperature over 10 minutes. ASTM D1003 was used to measure the haze of the sample plaques. The haze was 38%. The haze was much lower than that obtained in Comparative Example 1, demonstrating the effectiveness of the dispersant. In fact, optical microscopy shows carbon black particles less than 1 μm in size, with less than 20% of the carbon black present in the form of aggregates greater than 1 μm.

[0057] Comparative Example 3 The blends were made from a copolymer of VDF / HFP (15% HFP by weight) and the nucleating additive PTFE with a discrete particle size of 200 nm (0.05% by weight of the blend) (wet aqueous blend). Both materials were used in latex form. They were mixed in a centrifugal planetary mixer to produce a latex blend, which was then dried in an oven at 80°C for 12 hours. The resulting powder was compression molded into 1 mm thick plaques at 230°C under 5 MT pressure and cooled to room temperature over 10 minutes. A 1 mm control plaque of pure VDF / HFP copolymer was also compression molded under the same conditions. ASTM D1003 was used to measure the haze of the sample plaques. The haze of the pure copolymer was 72%, while the haze of the copolymer-PTFE blend was 61%. The reduction in haze with the addition of PTFE indicates that it acts as a nucleating additive, producing small alpha crystals that do not diffract light as much. However, there is a limit to the reduction in haze, which we speculate is due to poor dispersion of the 200 nm PTFE particles, which are likely to agglomerate into particles larger than 1 μm, as observed with carbon black.

[0058] Example 3 The blend was made from a copolymer of VDF / HFP (15 wt% HFP), nucleating additive PTFE, 200 nm discrete particle size (0.05 wt% of the blend), and Plexiglas V825-100 acrylic polymer (9.95 wt% of the blend) from Arkema. The VDF / HFP copolymer and PTFE latex were first mixed in a centrifugal planetary mixer to produce a latex blend, which was then dried in an oven at 80°C for 12 hours. The resulting dry powder was then blended (dried) with the acrylic polymer in a twin-screw extruder at 230°C to produce pellets. The pellets were compression molded into 1 mm thick plaques at 230°C under 5 MT pressure and cooled to room temperature over 10 minutes. ASTM D1003 was used to measure the haze of the sample plaques. The haze was 36%. This was much lower than that obtained in Comparative Example 3, demonstrating the effectiveness of the dispersant. We speculate that the dispersant helps break up agglomerates of the 200 nm discrete PTFE particles.

Claims

1. 1. A composition comprising: a. a PVDF copolymer, wherein at least one comonomer is selected from hexafluoropropene, 2,3,3,3-tetrafluoropropylene, 3,3,3-trifluoropropene, and VDF constitutes greater than 60% of all monomers; and b. 0.005-5% of one or more inorganic or polymeric nucleating additives, and c. 0.1 to 20% of one or more dispersing agents selected from the group of acrylic polymers and polyesters Including, an optical haze of less than 40% according to ASTM D1003 for a 1 mm thick part made by compression molding at 230°C; A composition wherein the nucleating additive is present as particles, and when the composition is observed using an optical microscope, more than 50% of the particles by number have a size of less than 5 μm.

2. The composition of claim 1 comprising 1 to 15% of one or more dispersants.

3. 3. The composition of claim 1, wherein the nucleating additive is present as particles, and more than 70% of the particles have a size less than 2 μm.

4. 3. The composition of claim 1, wherein the nucleating additive has an average particle size of less than 2 μm.

5. 3. The composition of claim 1 or 2, wherein the nucleating additive is selected from the group of inorganic particles, organic dyes, benzene derivatives, fluorinated polymers, crosslinked polymer particles, and combinations thereof.

6. 6. The composition of claim 5, wherein the inorganic particles are selected from carbon black, activated carbon, silica, clay, aluminosilicates, talc, mica, calcium carbonate, titania, and combinations thereof.

7. The composition of claim 5 , wherein the organic dye is selected from flavanthrones, idanthrones, perienes, quinophthalones, phthalocyanines, and combinations thereof.

8. The composition of claim 5, wherein the fluorinated polymer is selected from polytetrafluoroethylene polymers and copolymers.

9. 6. The composition of claim 5, wherein the crosslinked polymer particles are selected from polymers made by suspension or emulsion polymerization in the presence of a crosslinking monomer.

10. 3. The composition of claim 1, wherein the dispersing agent is selected from one or more plasticizers.

11. 11. The composition of claim 10, wherein the plasticizer is selected from the group consisting of acrylics, styrenes, polyesters, and combinations thereof.

12. 12. The composition of claim 11, wherein the acrylic is selected from poly(methyl methacrylate) oligomers, polymers, and copolymers.

13. 12. The composition of claim 11, wherein the polyester is selected from the group of polyethylene glycol, polypropylene glycol, and blends thereof.

14. A method for preparing a composition according to any one of claims 1 to 13, comprising the steps of: d. Mixing the nucleating additive with the dispersing agent in a mixer or extruder e. Mixing the blend of (d) with a VDF-based copolymer in an extruder. A method comprising:

15. A method for preparing a composition according to any one of claims 1 to 13, comprising the steps of: f. Mixing the VDF-based copolymer latex with a nucleating additive and / or a dispersant. g. Drying the latex into a solid material A method comprising:

16. 3. An article comprising the composition of claim 1 or 2, said article being a film, a sheet, a rod, a multi-layer part, or any other shape and configuration.

17. 17. The article of claim 16, wherein the article is a melt-processed article.

18. 17. Use of the article of claim 16 for wire and cable, oil and gas, consumer electronics, photovoltaic cells, protective films, packaging, medical devices.

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