WO2018077968A1 - Fluoropolymer composition comprising calcium oxide or calcium carbonate for thermoformed window shades - Google Patents
Fluoropolymer composition comprising calcium oxide or calcium carbonate for thermoformed window shades Download PDFInfo
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- WO2018077968A1 WO2018077968A1 PCT/EP2017/077343 EP2017077343W WO2018077968A1 WO 2018077968 A1 WO2018077968 A1 WO 2018077968A1 EP 2017077343 W EP2017077343 W EP 2017077343W WO 2018077968 A1 WO2018077968 A1 WO 2018077968A1
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- fluoropolymer composition
- polymer
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K3/00—Use of inorganic substances as compounding ingredients
- C08K3/18—Oxygen-containing compounds, e.g. metal carbonyls
- C08K3/20—Oxides; Hydroxides
- C08K3/22—Oxides; Hydroxides of metals
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J5/00—Manufacture of articles or shaped materials containing macromolecular substances
- C08J5/18—Manufacture of films or sheets
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K3/00—Use of inorganic substances as compounding ingredients
- C08K3/18—Oxygen-containing compounds, e.g. metal carbonyls
- C08K3/24—Acids; Salts thereof
- C08K3/26—Carbonates; Bicarbonates
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B64—AIRCRAFT; AVIATION; COSMONAUTICS
- B64C—AEROPLANES; HELICOPTERS
- B64C1/00—Fuselages; Constructional features common to fuselages, wings, stabilising surfaces or the like
- B64C1/14—Windows; Doors; Hatch covers or access panels; Surrounding frame structures; Canopies; Windscreens accessories therefor, e.g. pressure sensors, water deflectors, hinges, seals, handles, latches, windscreen wipers
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2323/00—Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers
- C08J2323/02—Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers not modified by chemical after treatment
- C08J2323/04—Homopolymers or copolymers of ethene
- C08J2323/08—Copolymers of ethene
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2327/00—Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Derivatives of such polymers
- C08J2327/02—Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Derivatives of such polymers not modified by chemical after-treatment
- C08J2327/12—Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Derivatives of such polymers not modified by chemical after-treatment containing fluorine atoms
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2327/00—Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Derivatives of such polymers
- C08J2327/02—Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Derivatives of such polymers not modified by chemical after-treatment
- C08J2327/12—Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Derivatives of such polymers not modified by chemical after-treatment containing fluorine atoms
- C08J2327/18—Homopolymers or copolymers of tetrafluoroethylene
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K3/00—Use of inorganic substances as compounding ingredients
- C08K3/18—Oxygen-containing compounds, e.g. metal carbonyls
- C08K3/20—Oxides; Hydroxides
- C08K3/22—Oxides; Hydroxides of metals
- C08K2003/2206—Oxides; Hydroxides of metals of calcium, strontium or barium
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K3/00—Use of inorganic substances as compounding ingredients
- C08K3/18—Oxygen-containing compounds, e.g. metal carbonyls
- C08K3/24—Acids; Salts thereof
- C08K3/26—Carbonates; Bicarbonates
- C08K2003/265—Calcium, strontium or barium carbonate
Definitions
- the present invention pertains to a fluoropolymer composition (C)
- composition (C) for the preparation of sheets for thermoformed or injection molded window shades and other body panels. These articles or parts can be used in vehicles, e.g. airplanes, trains, buses or the like.
- PVF polyvinylfluoride
- PEKK polyaryletherketoneketone
- structures of PVF/PEKK which can be shaped into their final desired configuration, such as structures for aircraft interiors, and backfilled with a moulding resin.
- said laminates suffer from high manufacturing costs, multiple process steps, low yields, and color shifts in processing from exposing the low temperature PVF to the processing temperature of PEKK.
- thermoformable monolayer fluoromaterial sheets of appropriate thickness would be considered as suitable candidates for the preparation of window shades, eliminating the need for adhesives and limiting the risks of colour shift during exposure to high temperature.
- ECTFE and ETFE have been extensively employed in several fields of use, thanks to their chemical resistance, wide continuous usage temperature range and thermal ageing resistance, good fire resistance with high limiting oxygen index, very low small molecules permeation, and excellent corrosion resistance.
- US 5328948 (AUSIMONT, USA, INC.) 7/12/1994 pertains to the stabilization of ethylene/chlorotrifluoroethylene copolymers using a combination of an effective amount of a ionomer, and of an antioxidant selected from notably phosphate derivatives.
- an ethylene- acrylic acid copolymer metal salt notably commercially available from Allied-Signal as Aclyn ® grade, or styrene/sulfonated styrene copolymer in its salified form were employed in preferred embodiments.
- WO2014/187758 SOLVAY SPECIALTY POLYMERS ITALY 27/1 1/2014 discloses a stabilizer package comprising an antioxidant and a
- polyelectrolyte preferably selected from the group consisting of poly(meth)acrylic acid metal or ammonium salts, which can improve the properties of ECTFE when melt processed at high temperatures.
- the materials to be used in vehicle interiors have to fulfil certain specific requirements in terms of flammability and smoke emissions when exposed to a flame.
- thermoformable articles are made efficient and economical.
- At least one polymer (A) comprising recurring units derived from ethylene (E) and at least one of chlorotrifluoroethylene (CTFE) and
- TFE tetrafluoroethylene
- the fluoropolymer composition (C) of the present invention presents the ability to be processed into extruded thermoformable or injection molded articles having excellent surface properties and reduced smoke toxicity, which makes the composition (C) well-suited for window shades to be used in vehicles, for example aircrafts.
- the composition also presents an advantageous set of properties, including chemical, UV, mechanical and flammability resistance performances.
- the combination of the polymer (A) and at least one acid scavenger (AS) allows obtaining sheets of high quality, in terms of thickness, homogeneity and texture.
- the invention further pertains to a method of making a sheet (S) from the fluoropolymer composition (C) comprising a step of extruding the fluoropolymer composition (C) by means of an extruder.
- Still another object of the present invention is a method for making a shaped article including using the sheet (S) made from a fluoropolymer composition (C), said method comprising thermoforming or injection moulding a sheet (S) made from the fluoropolymer composition (C).
- Embodiments wherein polymer (A) essentially consists of recurring units (a), (b) and optionally (c), and preferably of recurring units (a) and (b), as above detailed, are generally preferred. End chain, defects and minor amounts of monomer impurities leading to recurring units different from those above mentioned (typically, ⁇ 0.1 % moles, with respect to the total amount of recurring units) may be tolerated, without these substantially affecting the properties of polymer (A).
- CTFE chlorotrifluoroethylene
- TFE tetrafluoroethylene
- (c) optionally, recurring units derived from one or more fluorinated and/or hydrogenated comonomer(s), in an up to 3 mol.%, preferably up to 2 mol. %
- the total amount of recurring units (a), (b) and (c) being equal to 100 mol.%, based on the total number of moles of recurring units of said polymer (A).
- the polymer (A) consists essentially in recurring units (a), (b) and optionally (c). According to a most preferred embodiment, the polymer (A) consist essentially in recurring units (a) and (b). End chain, defects and minor amounts of monomer impurities leading to recurring units different from those above mentioned (for example ⁇ 0.1 mol %, with respect to the total amount of recurring units) may be tolerated, without these substantially affecting the properties of polymer (A).
- the comonomer is generally a hydrogenated comonomer selected from the group of the (meth)acrylic monomers. More preferably, the hydrogenated comonomer is selected from the group of the hydroxyalkylacrylate comonomers, such as hydroxyethylacrylate, hydroxypropylacrylate and
- the polymer (A) suitable in the fluoropolymer composition of the invention presents a melting temperature Tm greater than 220°C, preferably greater than 225°C, even greater than 230°C, preferably greater than 235°C.
- the melting temperature (Tm) of the polymer (A) can for example be determined by Differential Scanning Calorimetry (DSC) at a heating rate of 10°C/min, according to ASTM D 3418.
- the polymer (A) suitable in the fluoropolymer composition of the invention presents a heat of fusion of at least 35 J/g, preferably of at least 37 J/g, more preferably of at least 40 J/g, as determined by Differential Scanning Calorimetry (DSC) at a heating rate of 10°C/min, according to ASTM D 3418.
- DSC Differential Scanning Calorimetry
- fluoropolymer composition of the invention presents a heat of fusion of at most 55 J/g, preferably of at most 53 J/g, more preferably of at most 50 J/g, as determined by Differential Scanning Calorimetry (DSC) at a heating rate of 10°C/min, according to ASTM D 3418.
- DSC Differential Scanning Calorimetry
- fluoropolymer composition of the invention presents a melt flow rate ranging from 0.1 to 35 g/10 min, as measured according to ASTM D 3275- 81 at 275°C and 2.16 Kg, .
- melt flow rate of the polymer (A), as measured according to ASTM D 3275-08 at 275°C and 2.16 Kg, ranges from 0.2 to 2 g/10 min.
- ECTFE copolymers i.e. copolymers of ethylene
- CTFE and optionally a third monomer (c) are preferred.
- ECTFE copolymers which have been found to give particularly good results are those consisting essentially of:
- the amount of recurring units (a) and (b) being equal to 100 mol. %, based on the total number of moles of recurring units of the polymer (A).
- Polymer (A) may comprise additional optional ingredients, such as
- the fluoropolymer composition (C) of the invention comprises at least one acid scavenger (AS) selected from the group consisting of calcium carbonate and calcium oxide.
- AS acid scavenger
- the acid scavenger (AS) is present in the fluoropolymer composition (C) in an amount of from 10 to 40 wt. %, preferably of from 1 1 to 25 wt. %, and more preferably 12 to 16 wt. %, based on the weight of polymer (A).
- the fluoropolymer [0036] According to one aspect of the present invention, the fluoropolymer
- the colorant (COL) is a white
- the amount of colorant (COL) in the fluoropolymer composition (C), based on the total weight of polymer (A), may be of from 2 to 20 wt. %, more preferably from 10 to 16 wt. %.
- T1O2 may be mixed with any conventional colorant such as a pigment, dye or a dispersed dye to impart the required color to the fluoropolymer composition.
- any conventional colorant such as a pigment, dye or a dispersed dye to impart the required color to the fluoropolymer composition.
- the present invention relates to a
- fluoropolymer composition (C) comprising:
- At least one polymer (A) comprising recurring units derived from ethylene and at least one of chlorotrifluoroethylene (CTFE) and tetrafluoroethylene (TFE) ;
- - at least one colorant preferably being a white pigment, more preferably being T1O2.
- the invention further pertains to a process for manufacturing the
- composition of the invention is particularly suitable for manufacturing films, sheets or other finished articles.
- the fluoropolymer composition (C) according to the invention as above detailed can be processed by all the conventional techniques for the conversion in the molten state.
- the invention thus further pertains to a method of making a sheet (S) from the fluoropolymer composition (C) as above detailed, said method comprising processing the composition (C) in the molten state, preferably by extrusion.
- the sheet (S) made from the fluoropolymer composition (C) of the present invention is characterized by improved thermal stability and reduced production of gases generated by combustion, as measured according to BSS7239 (test method for toxic gas generation by materials on
- BSS7239 is a standard procedure established by Boeing for measuring the amount of gases generated in a specified, calibrated smoke chamber during standard rate of smoke generation testing (ASTM E 662), in both flaming combustion and non-flaming pyrolytic decomposition test modes. The amount of the following gases is measured in this procedure: CO (carbon monoxide), HF (hydrogen fluoride), HCI (hydrogen chloride), NOx (nitrogen oxides - both NO, nitric oxide, and NO2, nitrogen dioxide, are detected), SO2 (sulfur dioxide) and HCN (hydrogen cyanide).
- CO carbon monoxide
- HF hydrogen fluoride
- HCI hydrogen chloride
- NOx nitrogen oxides - both NO, nitric oxide, and NO2, nitrogen dioxide, are detected
- SO2 sulfur dioxide
- HCN hydrogen cyanide
- the sheet (S) obtained from a fluoropolymer composition (C) of the invention is characterized by an improved thermal stability, having a degradation temperature, measured by TGA (ASTM E1 131 -08) with a ramp of 20° C/min in N2, which is higher than that of polymers (A) stabilized with different acid scavengers.
- the thickness of the sheet (S) obtained from a fluoropolymer composition (C) of the invention may range from 0.5 to 2.5 mm, preferably from 0.8 to 1.8 mm, more preferably from 1 to 1.5 mm.
- Still another object of the present invention is a method for making a
- thermoforming or injection moulding the sheet (S) made from a fluoropolymer composition (C) according to the invention.
- thermoforming is used to describe a method that comprises the sequential or simultaneous heating and forming of a material onto a mold, wherein the material is originally in the form of a sheet (e.g., film, layer, and the like) and is formed into a desired shape. Once the desired shape has been obtained, the formed article (e.g., window shade) is cooled below its glass transition temperature.
- a sheet e.g., film, layer, and the like
- injection moulding is defined as a conventional injection moulding
- the article so obtained advantageously exhibits outstanding mechanical properties, while ensuring outstanding opacity, superior thermal stability and reduced smoke toxicity.
- the article of the invention is particularly suitable for use in various
- window shades and other body panels for use in vehicles, e.g., airplanes, trains, buses or the like.
- CaCO3 (Calcium carbonate): Hubercarb® W3N available from J. M. Huber
- CaO Calcium oxide
- pulverized BET surface area of 2.0 m2/g
- NW-2200 Aluminium magnesium carbonate eptahydroxide (CHzAIMgO). available from Kyowa Chemical Industry Co.
- C.6 were prepared by melt blending the ingredients listed in Table 1 in a twin screw extruder. The barrel temperatures were about 250° C and screw speed was 250 rpm. Upon exiting the extruder, the molten compound was quenched in a water bath and pelletized.
- Films were prepared on a Brabender Intelli-torque 19 mm single screw extruder with a 100 mm ribbon die for appearance evaluations. Melt temperatures were in the range of 240 to 260 °C, screw speed was set at 50 rpm and puller roll speed adjusted from 40 to 60% in order to obtain a 50 micron thick film.
- compositions 1 and 2 and comparative compositions C.1 to C.6 were converted to films of 0.002 inch thickness (0.050 mm) by extrusion according to the method above detailed.
- the quality of the films so obtained was evaluated visually in terms of color (white, off white, beige), of opacity (clear, opaque, translucent) and of presence of imperfections and rated 0 to 3, where 0 is bad overall quality and 3 is good overall quality).
- Sheets prepared from compositions according to the invention, as well as sheets containing ZnO as acid scavenger resulted in quite good quality extruded sheets, while the compositions including the ECTFE polymer an other acid scavengers did not meet the quality requirements.
- compositions 1 and 2 and comparative compositions C.1 to C.3 were compression moulded into 1.0 mm plaques for smoke toxicity testing according to Boeing BSS7239 method, flaming mode.
- compositions comprising ECTFE polymer, titanium dioxide and calcium carbonate or calcium oxide have an overall emission of the toxic gases HCI and HF which is much lower than that of comparative compositions which include ZnO as acid scavenger, with or without T1O2 (C.1 and C.2, respectively) or of comparative composition C.3 which includes only the ECTFE polymer and T1O2.
- thermo degradation temperatures of samples of compositions 1 and 2 and of the comparative compositions C.1 to C.3 were determined by a Thermogravimetric Analysis instrument (TGA).
- Thermogravimetric analysis is often used to determine thermal stability by means of weight-loss decomposition profiles as a function of temperature. This was carried out using a TA instruments TGA Q500, ramp: 10° C./min, max temp: 800° C, in nitrogen.
- compositions according to the present invention have a higher degradation temperature in comparison with compositions including the acid scavenger ZnO or including only the ECTFE polymer and T1O2.
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Abstract
The present invention pertains to a fluoropolymer composition (C) comprising a polymer (A) of ethylene and tetrafluoroethylene and/or chlorotrifluoroethylene, and a certain amount of specific acid scavenger (AS), optionally a colorant,and to the use thereof for the preparation of sheets for thermoformed or injection moulded window shades and other body panels for use in vehicles, e.g., airplanes, trains, buses or the like.
Description
Description
FLUOROPOLYMER COMPOSITION COMPRISING CALCIUM OXIDE OR CALCIUM CARBONATE FOR THERMOFORMED WINDOW SHADES
Related applications
[0001] This application claims priority to U.S. provisional application
No. 62/413,353 - filed October 26, 2016 and to European application No. 17153294.8 - filed January 26, 2017, the whole content of each of these applications being incorporated herein by reference for all purposes.
Technical Field
[0002] The present invention pertains to a fluoropolymer composition (C)
comprising at least one polymer of ethylene and tetrafluoroethylene and/or chlorotrifluoroethylene, and a certain amount of specific acid scavenger (AS), optionally colorants. The present invention also relates to the use of the composition (C) for the preparation of sheets for thermoformed or injection molded window shades and other body panels. These articles or parts can be used in vehicles, e.g. airplanes, trains, buses or the like.
Background Art
[0003] Current window shades in commercial passenger vehicles, aircrafts in particular, are extremely complex thermoformed laminates of
polyvinylfluoride (PVF) and polyaryletherketoneketone (PEKK).
[0004] US5304413 (DU PONT DE NEMOURS) 19/4/1994 discloses laminar
structures of PVF/PEKK which can be shaped into their final desired configuration, such as structures for aircraft interiors, and backfilled with a moulding resin.
[0005] However, said laminates suffer from high manufacturing costs, multiple process steps, low yields, and color shifts in processing from exposing the low temperature PVF to the processing temperature of PEKK.
[0006] As an alternative to PVF/PEKK laminates, thermoformable monolayer fluoromaterial sheets of appropriate thickness would be considered as suitable candidates for the preparation of window shades, eliminating the
need for adhesives and limiting the risks of colour shift during exposure to high temperature.
[0007] ECTFE and ETFE have been extensively employed in several fields of use, thanks to their chemical resistance, wide continuous usage temperature range and thermal ageing resistance, good fire resistance with high limiting oxygen index, very low small molecules permeation, and excellent corrosion resistance.
[0008] Nevertheless, exposure to harsh thermal conditions during processing in the molten state, such as during extrusion, or during thermoforming might lead to thermal decomposition of ECTFE and ETFE.
[0009] It is generally understood that the mechanism of decomposition involves both radical generation and direct dehydrohalogenation, both of which might finally generate HF and also HCI in the case of ECTFE. As a whole, the result of thermal instability leads to poor processibility, yellow to brownish color in the material and bubbles and gels in films and sheets.
[0010] To address the thermal instability of ECTFE and ETFE, particularly when intended to be processed in the molten state, stabilizers are added to the materials before they are extruded and converted to films.
[001 1] Thus, US 5328948 (AUSIMONT, USA, INC.) 7/12/1994 pertains to the stabilization of ethylene/chlorotrifluoroethylene copolymers using a combination of an effective amount of a ionomer, and of an antioxidant selected from notably phosphate derivatives. As ionomers, an ethylene- acrylic acid copolymer metal salt, notably commercially available from Allied-Signal as Aclyn® grade, or styrene/sulfonated styrene copolymer in its salified form were employed in preferred embodiments.
[0012] WO2014/187758 (SOLVAY SPECIALTY POLYMERS ITALY) 27/1 1/2014 discloses a stabilizer package comprising an antioxidant and a
polyelectrolyte, preferably selected from the group consisting of poly(meth)acrylic acid metal or ammonium salts, which can improve the properties of ECTFE when melt processed at high temperatures.
[0013] Nevertheless, the addition of acid scavengers to fluoropolymers can cause quality issues in the materials when melt processed at high temperatures
for preparing films of sheets, such as uneven distribution of the material, generation of holes, surface and texture imperfections.
[0014] Moreover, the materials to be used in vehicle interiors have to fulfil certain specific requirements in terms of flammability and smoke emissions when exposed to a flame.
[0015] There accordingly remains a continuing need in the art for materials useful in manufacture of articles that have a low release of gases on combustion and that have combustion products with low toxicity. In addition, it would be advantageous if manufacture of thermoformable articles is made efficient and economical.
Summary of invention
[0016] It is an object of the invention a fluoropolymer composition (C) comprising:
- at least one polymer (A) comprising recurring units derived from ethylene (E) and at least one of chlorotrifluoroethylene (CTFE) and
tetrafluoroethylene (TFE) ;
- from 10 to 40 wt.%, based on the weight of polymer (A), of at least one acid scavenger (AS) selected from the group consisting of calcium carbonate and calcium oxide.
[0017] The fluoropolymer composition (C) of the present invention presents the ability to be processed into extruded thermoformable or injection molded articles having excellent surface properties and reduced smoke toxicity, which makes the composition (C) well-suited for window shades to be used in vehicles, for example aircrafts. The composition also presents an advantageous set of properties, including chemical, UV, mechanical and flammability resistance performances.
[0018] The combination of the polymer (A) and at least one acid scavenger (AS) allows obtaining sheets of high quality, in terms of thickness, homogeneity and texture.
[0019] The invention further pertains to a method of making a sheet (S) from the fluoropolymer composition (C) comprising a step of extruding the fluoropolymer composition (C) by means of an extruder.
[0020] Still another object of the present invention is a method for making a shaped article including using the sheet (S) made from a fluoropolymer composition (C), said method comprising thermoforming or injection moulding a sheet (S) made from the fluoropolymer composition (C).
Description of embodiments
[0021] Embodiments wherein polymer (A) essentially consists of recurring units (a), (b) and optionally (c), and preferably of recurring units (a) and (b), as above detailed, are generally preferred. End chain, defects and minor amounts of monomer impurities leading to recurring units different from those above mentioned (typically, <0.1 % moles, with respect to the total amount of recurring units) may be tolerated, without these substantially affecting the properties of polymer (A).
[0022] Polymer (A) of the fluoropolymer composition (C) of the invention
comprises:
(a) recurring units derived from of ethylene (E) in an amount ranging from 45 to 55 mol. %, preferably from 47 to 53 mol. %;
(b) recurring units derived from at least one of chlorotrifluoroethylene (CTFE), tetrafluoroethylene (TFE) or mixture thereof, in an amount ranging from 55 to 45 mol.%, preferably from 53 to 47 mol. %,
(c) optionally, recurring units derived from one or more fluorinated and/or hydrogenated comonomer(s), in an up to 3 mol.%, preferably up to 2 mol. %
the total amount of recurring units (a), (b) and (c) being equal to 100 mol.%, based on the total number of moles of recurring units of said polymer (A).
[0023] According to a preferred embodiment, the polymer (A) consists essentially in recurring units (a), (b) and optionally (c). According to a most preferred embodiment, the polymer (A) consist essentially in recurring units (a) and (b). End chain, defects and minor amounts of monomer impurities leading to recurring units different from those above mentioned (for example < 0.1 mol %, with respect to the total amount of recurring units) may be
tolerated, without these substantially affecting the properties of polymer (A).
[0024] When the polymer (A) comprises recurring units (c), the comonomer is generally a hydrogenated comonomer selected from the group of the (meth)acrylic monomers. More preferably, the hydrogenated comonomer is selected from the group of the hydroxyalkylacrylate comonomers, such as hydroxyethylacrylate, hydroxypropylacrylate and
(hydroxy)ethylhexylacrylate, and alkyl acrylate comonomers, such as n- butyl acrylate.
[0025] According to an embodiment, the polymer (A) suitable in the fluoropolymer composition of the invention presents a melting temperature Tm greater than 220°C, preferably greater than 225°C, even greater than 230°C, preferably greater than 235°C. The melting temperature (Tm) of the polymer (A) can for example be determined by Differential Scanning Calorimetry (DSC) at a heating rate of 10°C/min, according to ASTM D 3418.
[0026] According to an embodiment, the polymer (A) suitable in the fluoropolymer composition of the invention presents a heat of fusion of at least 35 J/g, preferably of at least 37 J/g, more preferably of at least 40 J/g, as determined by Differential Scanning Calorimetry (DSC) at a heating rate of 10°C/min, according to ASTM D 3418.
[0027] According to another embodiment, the polymer (A) suitable in the
fluoropolymer composition of the invention presents a heat of fusion of at most 55 J/g, preferably of at most 53 J/g, more preferably of at most 50 J/g, as determined by Differential Scanning Calorimetry (DSC) at a heating rate of 10°C/min, according to ASTM D 3418.
[0028] According to another embodiment, the polymer (A) suitable in the
fluoropolymer composition of the invention presents a melt flow rate ranging from 0.1 to 35 g/10 min, as measured according to ASTM D 3275- 81 at 275°C and 2.16 Kg, .
[0029] In a preferred embodiment, the melt flow rate of the polymer (A), as
measured according to ASTM D 3275-08 at 275°C and 2.16 Kg, ranges from 15 to 27 g/10 min.
[0030] In another preferred embodiment, the melt flow rate of the polymer (A), as measured according to ASTM D 3275-08 at 275°C and 2.16 Kg, ranges from 0.2 to 2 g/10 min.
[0031] Among polymers (A), ECTFE copolymers, i.e. copolymers of ethylene and
CTFE and optionally a third monomer (c) are preferred.
ECTFE copolymers which have been found to give particularly good results are those consisting essentially of:
(a) recurring units derived from ethylene (E) in an amount of 47 to 53 mol.
%;
(b) recurring units derived from chlorotrifluoroethylene (CTFE) in an amount of 53 to 47 mol. %,
the amount of recurring units (a) and (b) being equal to 100 mol. %, based on the total number of moles of recurring units of the polymer (A).
[0032] Polymer (A) may comprise additional optional ingredients, such as
ionomers, polyelectrolytes and antioxidants, as for example the ones described in WO 2014/187758 and US 5328948, incorporated herein by reference.
[0033] The fluoropolymer composition (C) of the invention comprises at least one acid scavenger (AS) selected from the group consisting of calcium carbonate and calcium oxide.
[0034] The acid scavenger (AS) is present in the fluoropolymer composition (C) in an amount of from 10 to 40 wt. %, preferably of from 1 1 to 25 wt. %, and more preferably 12 to 16 wt. %, based on the weight of polymer (A).
[0035] The addition of calcium carbonate and/or calcium oxide to the polymer (A) in the amount as above detailed has the beneficial effect of providing compositions that can be converted by extrusion to high quality sheets, which have homogeneous structure and texture, having at most very few imperfections, which represents an important feature of this invention.
[0036] According to one aspect of the present invention, the fluoropolymer
composition (C) further comprises at least one colorant (COL).
[0037] According to a preferred embodiment, the colorant (COL) is a white
pigment, more preferably T1O2.
[0038] The amount of colorant (COL) in the fluoropolymer composition (C), based on the total weight of polymer (A), may be of from 2 to 20 wt. %, more preferably from 10 to 16 wt. %.
[0039] T1O2 may be mixed with any conventional colorant such as a pigment, dye or a dispersed dye to impart the required color to the fluoropolymer composition.
[0040] The addition of a colorant (COL) to the fluoropolymer composition (C) present the technical effect of providing opacity, even at a low sheet thickness. In other words, no light is transmitted through the material when a colorant is used.
[0041] In a preferred embodiment, the present invention relates to a
fluoropolymer composition (C) comprising:
- at least one polymer (A) comprising recurring units derived from ethylene and at least one of chlorotrifluoroethylene (CTFE) and tetrafluoroethylene (TFE) ;
- from 10 to 40 wt. %, based on the weight of polymer (A), of at least one acid scavenger (AS) selected from the group consisting of calcium carbonate and calcium oxide; and
- at least one colorant (COL), preferably being a white pigment, more preferably being T1O2.
[0042] The invention further pertains to a process for manufacturing the
fluoropolymer composition (C) as above described, the process
comprising mixing the at least one polymer (A), the at least one acid scavenger (AS) and optionally the at least one the colorant (COL).
[0043] The composition of the invention is particularly suitable for manufacturing films, sheets or other finished articles.
[0044] The fluoropolymer composition (C) according to the invention as above detailed can be processed by all the conventional techniques for the conversion in the molten state.
[0045] The invention thus further pertains to a method of making a sheet (S) from the fluoropolymer composition (C) as above detailed, said method comprising processing the composition (C) in the molten state, preferably by extrusion.
[0046] The sheet (S) made from the fluoropolymer composition (C) of the present invention is characterized by improved thermal stability and reduced production of gases generated by combustion, as measured according to BSS7239 (test method for toxic gas generation by materials on
combustion). BSS7239 is a standard procedure established by Boeing for measuring the amount of gases generated in a specified, calibrated smoke chamber during standard rate of smoke generation testing (ASTM E 662), in both flaming combustion and non-flaming pyrolytic decomposition test modes. The amount of the following gases is measured in this procedure: CO (carbon monoxide), HF (hydrogen fluoride), HCI (hydrogen chloride), NOx (nitrogen oxides - both NO, nitric oxide, and NO2, nitrogen dioxide, are detected), SO2 (sulfur dioxide) and HCN (hydrogen cyanide).
[0047] Moreover, the sheet (S) obtained from a fluoropolymer composition (C) of the invention is characterized by an improved thermal stability, having a degradation temperature, measured by TGA (ASTM E1 131 -08) with a ramp of 20° C/min in N2, which is higher than that of polymers (A) stabilized with different acid scavengers.
[0048] The thickness of the sheet (S) obtained from a fluoropolymer composition (C) of the invention may range from 0.5 to 2.5 mm, preferably from 0.8 to 1.8 mm, more preferably from 1 to 1.5 mm.
[0049] Still another object of the present invention is a method for making a
shaped article including thermoforming or injection moulding the sheet (S) made from a fluoropolymer composition (C) according to the invention.
[0050] It is generally noted that the term "thermoforming" is used to describe a method that comprises the sequential or simultaneous heating and forming of a material onto a mold, wherein the material is originally in the form of a sheet (e.g., film, layer, and the like) and is formed into a desired shape. Once the desired shape has been obtained, the formed article (e.g., window shade) is cooled below its glass transition temperature.
[0051] The term "injection moulding" is defined as a conventional
injection moulding process involving the rapid injection of a moldable material into a cavity formed by at least a pair of closed mold members.
[0052] All the features described above for components polymer (A), acid scavenger (AS) and colorant (COL) of the fluoropolymer composition (C) are also applicable here as preferred embodiments of the sheet made from the fluoropolymer composition (C) and the article made from the sheet (S).
[0053] It has been found that the article so obtained advantageously exhibits outstanding mechanical properties, while ensuring outstanding opacity, superior thermal stability and reduced smoke toxicity.
[0054] The article of the invention is particularly suitable for use in various
applications such as in window shades and other body panels for use in vehicles, e.g., airplanes, trains, buses or the like.
[0055] Should the disclosure of any patents, patent applications, and publications which are incorporated herein by reference conflict with the description of the present application to the extent that it may render a term unclear, the present description shall take precedence.
[0056] The invention will be now described with reference to the following
examples, whose purpose is merely illustrative and not intended to limit scope of the invention.
[0057] EXAMPLES
[0058] RAW MATERIALS
Polymer (A1 ): HALAR® 500 LC, a ECTFE polymer, 50/50 molar ratio
E/CTFE with melting temperature of 242 °C and heat of fusion of 42 J/g commercially available from Solvay Specialty Polymers
CaCO3 (Calcium carbonate): Hubercarb® W3N available from J. M. Huber
Corp
CaO (Calcium oxide), pulverized (BET surface area of 2.0 m2/g) available from Mississippi Lime Company
ZnO (Zinc oxide): Zoco 102 available from Zochem
CaSiO3 (Wollastonite):Wollastonite Nyad 400 from Imerys.
NW-2200, Aluminium magnesium carbonate eptahydroxide (CHzAIMgO). available from Kyowa Chemical Industry Co.
KenReact TTS/H, available from Kenrich Petrochemicals
T1O2 Ti-Pure R-350 titanium dioxide available from Chemours
T1O2 Ti-Pure R-105 titanium dioxide available from Chemours
GENERAL PROCEDURE FOR PREPARING COMPOSITIONS
Examples 1 and 2 and comparative examples C.1 , C.2, C.3, C.4, C.5 and
C.6 were prepared by melt blending the ingredients listed in Table 1 in a twin screw extruder. The barrel temperatures were about 250° C and screw speed was 250 rpm. Upon exiting the extruder, the molten compound was quenched in a water bath and pelletized.
Table 1
Values are reported as percentages by weight (wt. %).
[0060] GENERAL PROCEDURE FOR PREPARING SHEETS
Films were prepared on a Brabender Intelli-torque 19 mm single screw extruder with a 100 mm ribbon die for appearance evaluations. Melt temperatures were in the range of 240 to 260 °C, screw speed was set at 50 rpm and puller roll speed adjusted from 40 to 60% in order to obtain a 50 micron thick film.
[0061] FILM PROPERTIES OF THE COMPOSITIONS
Compositions 1 and 2 and comparative compositions C.1 to C.6 were converted to films of 0.002 inch thickness (0.050 mm) by extrusion according to the method above detailed.
The quality of the films so obtained was evaluated visually in terms of color (white, off white, beige), of opacity (clear, opaque, translucent) and of presence of imperfections and rated 0 to 3, where 0 is bad overall quality and 3 is good overall quality).
The table 2 herein below summarizes the data obtained.
Table 2
Sheets prepared from compositions according to the invention, as well as sheets containing ZnO as acid scavenger resulted in quite good quality extruded sheets, while the compositions including the ECTFE polymer an other acid scavengers did not meet the quality requirements.
SMOKE TOXICITY OF THE COMPOSITIONS
Compositions 1 and 2 and comparative compositions C.1 to C.3 were compression moulded into 1.0 mm plaques for smoke toxicity testing according to Boeing BSS7239 method, flaming mode.
The results in ppm are summarized in table 3 here below.
Table 3
COMPOSITION 1 2 C.1 C.2 C.3
HCN <1 <1 <1 <1 <1
CO (1 ) 752 444 1017 490 474
CO (2) 657 479 647 451
NO/NO2 1 1 3 1 2
SO2 <1 <1 <1 <1 <1
HCI (1 ) 395 250 450 >500 >500
HCI (2) 400 275 450 >500 >500
HCI (3) 400 275 475
HF (1 ) 60 49 243 201 17
HF (2) 59 48 240 49
The results demonstrate that the compositions comprising ECTFE polymer, titanium dioxide and calcium carbonate or calcium oxide have an overall emission of the toxic gases HCI and HF which is much lower than that of comparative compositions which include ZnO as acid scavenger, with or without T1O2 (C.1 and C.2, respectively) or of comparative composition C.3 which includes only the ECTFE polymer and T1O2.
DEGRADATION TEMPERATURE OF THE COMPOSITIONS
The thermal degradation temperatures of samples of compositions 1 and 2 and of the comparative compositions C.1 to C.3 were determined by a Thermogravimetric Analysis instrument (TGA).
Thermogravimetric analysis (TGA) is often used to determine thermal stability by means of weight-loss decomposition profiles as a function of temperature. This was carried out using a TA instruments TGA Q500, ramp: 10° C./min, max temp: 800° C, in nitrogen.
The results are summarized in table 4 here below.
Table 4
The results demonstrate that the compositions according to the present invention have a higher degradation temperature in comparison with compositions including the acid scavenger ZnO or including only the
ECTFE polymer and T1O2.
Claims
Claim 1. A fluoropolymer composition (C) comprising:
- at least one polymer (A) comprising recurring units derived from ethylene (E) and at least one of chlorotrifluoroethylene (CTFE) and tetrafluoroethylene (TFE) ;
- from 10 to 40 wt. %, based on the weight of polymer (A), of at least one acid scavenger (AS) selected from the group consisting of calcium carbonate and calcium oxide.
Claim 2. The fluoropolymer composition (C) of claim 1 , wherein the polymer (A) comprise:
(a) 45 to 55 mol.% of recurring units derived from of ethylene (E) , preferably from 47 to 53 mol. %;
(b) 45 to 55 mol.% of recurring units derived from at least one of
chlorotrifluoroethylene (CTFE), tetrafluoroethylene (TFE) or mixture thereof, preferably from 53 to 47 mol. % ,
(c) 0 to 3 mol. % of recurring units derived from at least one fluorinated and/or hydrogenated monomer, preferably from 0 to 2 mol. %,
the total amount of recurring units (a), (b) and (c) being equal to 100 mol. %, based on the total number of moles of recurring units of polymer (A).
Claim 3. The fluoropolymer composition (C) of claim 2, wherein the polymer (A) comprises recurring units derived from (meth)acrylic monomers as recurring units (c).
Claim 4. The fluoropolymer composition (C) of claim 2, wherein polymer (A) consists essentially in:
(a) 47 to 53 mol. %of recurring units derived from ethylene (E);
(b) 53 to 47 mol. % of recurring units derived from chlorotrifluoroethylene (CTFE),
the total amount of recurring units (a) and (b) being equal to 100 mol.%, based on the total number of moles of recurring units of said polymer (A).
Claim 5. The fluoropolymer composition (C) of any one of the preceding
claims, wherein the melting temperature of polymer (A), as measured by Differential Scanning Calorimetry (DSC) at a heating rate of 10°C/min, according to ASTM D 3418, is greater than 220°C, preferably greater than 225
°C, more preferably greater than230°C, still more preferably greater than 235° C.
Claim 6. The fluoropolymer composition (C) of any one of the preceding
claims ,wherein the heat of fusion of at least of polymer (A ), as measured by Differential Scanning Calorimetry (DSC) at a heating rate of 10°C/min, according to ASTM D 3418, is greater than 35 J/g, preferably greater than 37 J/g, more preferably greater than 40 J/g.
Claim 7. The fluoropolymer composition (C) of any one of the preceding
claims, wherein the melt flow rate of the ECTFE polymer, as measured according to the procedure of ASTM 3275-81 at 230°C, ranges from 0.1 to 35 g/10 min, preferably from 15 to 27 g/10 min or of from 0.2 to 2 g/10 min.
Claim 8. The fluoropolymer composition (C) of any one of the preceding
claims, wherein the acid scavenger (AS) is present in the fluoropolymer composition (C) in an amount ranging from 1 1 to 25 wt.%, more preferably ranging from 12 to 16 wt.%, based on the weight of polymer (A).
Claim 9. The fluoropolymer composition (C) of any one of the preceding
claims further comprising at least one colorant (COL).
Claim 10. The fluoropolymer composition (C) of claim 9, wherein the colorant (COL) is a white pigment, preferably T1O2.
Claim 1 1. The fluoropolymer composition (C) of anyone of claims 9 or 10, wherein the amount of colorant (COL) in the fluoropolymer composition (C), based on the total weight of polymer (A), ranges from 2 to 20 wt. %, preferably of from 10 to 16 wt.%.
Claim 12. A method of making a sheet (S) from the fluoropolymer composition (C) of any one of claims 1-1 1 , wherein themethod comprises a step of extruding the fluoropolymer composition (C) by means of an extruder.
Claim 13. A method for making a shaped article including thermoforming or injection moulding the sheet (S) of claim 12.
Claim 14. A shaped article comprising a thermoformed or injection moulded sheet (S) of claim 13.
Claim 15. The shaped article of claim 14 that is a window shade.
Claim 16. A vehicle comprising the shaped article of claims 14 or 15.
Claim 17. The vehicle of claim 16 wherein the vehicle is an airplane.
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US201662413353P | 2016-10-26 | 2016-10-26 | |
US62/413,353 | 2016-10-26 | ||
EP17153294 | 2017-01-26 | ||
EP17153294.8 | 2017-01-26 |
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PCT/EP2017/077343 WO2018077968A1 (en) | 2016-10-26 | 2017-10-25 | Fluoropolymer composition comprising calcium oxide or calcium carbonate for thermoformed window shades |
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Citations (6)
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US5304413A (en) | 1992-04-29 | 1994-04-19 | E. I. Du Pont De Nemours And Company | Molded PVF laminar structures |
US5328948A (en) | 1992-09-23 | 1994-07-12 | Ausimont, U.S.A., Inc. | Stabilization of halopolymers with ionomers |
EP1674503A1 (en) * | 2004-12-27 | 2006-06-28 | Carl Freudenberg KG | Thermoplastic vulcanizate with high temperature processing aid |
WO2014187758A1 (en) | 2013-05-21 | 2014-11-27 | Solvay Specialty Polymers Italy S.P.A. | Fluoropolymer composition |
CN105566737A (en) * | 2016-01-29 | 2016-05-11 | 芜湖佳宏新材料有限公司 | High-temperature-resistant PTC electric conduction composite |
WO2016128315A1 (en) * | 2015-02-11 | 2016-08-18 | Solvay Specialty Polymers Italy S.P.A. | Novel thermoprocessable fluoropolymer |
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2017
- 2017-10-25 WO PCT/EP2017/077343 patent/WO2018077968A1/en active Application Filing
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Publication number | Priority date | Publication date | Assignee | Title |
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US5304413A (en) | 1992-04-29 | 1994-04-19 | E. I. Du Pont De Nemours And Company | Molded PVF laminar structures |
US5328948A (en) | 1992-09-23 | 1994-07-12 | Ausimont, U.S.A., Inc. | Stabilization of halopolymers with ionomers |
EP1674503A1 (en) * | 2004-12-27 | 2006-06-28 | Carl Freudenberg KG | Thermoplastic vulcanizate with high temperature processing aid |
WO2014187758A1 (en) | 2013-05-21 | 2014-11-27 | Solvay Specialty Polymers Italy S.P.A. | Fluoropolymer composition |
WO2016128315A1 (en) * | 2015-02-11 | 2016-08-18 | Solvay Specialty Polymers Italy S.P.A. | Novel thermoprocessable fluoropolymer |
CN105566737A (en) * | 2016-01-29 | 2016-05-11 | 芜湖佳宏新材料有限公司 | High-temperature-resistant PTC electric conduction composite |
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