EP4638578A1 - Colored thermoplastic composition - Google Patents
Colored thermoplastic compositionInfo
- Publication number
- EP4638578A1 EP4638578A1 EP23821672.5A EP23821672A EP4638578A1 EP 4638578 A1 EP4638578 A1 EP 4638578A1 EP 23821672 A EP23821672 A EP 23821672A EP 4638578 A1 EP4638578 A1 EP 4638578A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- weight
- thermoplastic polymer
- colored thermoplastic
- microns
- polymer composition
- 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.)
- Pending
Links
Classifications
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L23/00—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
- C08L23/02—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
- C08L23/10—Homopolymers or copolymers of propene
- C08L23/12—Polypropene
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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
- C08K3/01—Use of inorganic substances as compounding ingredients characterized by their specific function
- C08K3/013—Fillers, pigments or reinforcing additives
-
- 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
- C08K3/02—Elements
- C08K3/04—Carbon
-
- 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
- C08K3/34—Silicon-containing compounds
-
- 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
- C08K9/00—Use of pretreated ingredients
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L23/00—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
- C08L23/02—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
- C08L23/04—Homopolymers or copolymers of ethene
- C08L23/06—Polyethylene
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L23/00—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
- C08L23/02—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
- C08L23/10—Homopolymers or copolymers of propene
- C08L23/14—Copolymers of propene
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L25/00—Compositions of, homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by an aromatic carbocyclic ring; Compositions of derivatives of such polymers
- C08L25/02—Homopolymers or copolymers of hydrocarbons
- C08L25/04—Homopolymers or copolymers of styrene
- C08L25/08—Copolymers of styrene
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L53/00—Compositions of block copolymers containing at least one sequence of a polymer obtained by reactions only involving carbon-to-carbon unsaturated bonds; Compositions of derivatives of such polymers
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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
- C08K2201/00—Specific properties of additives
- C08K2201/002—Physical properties
- C08K2201/005—Additives being defined by their particle size in general
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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
- C08K2201/00—Specific properties of additives
- C08K2201/016—Additives defined by their aspect ratio
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L2207/00—Properties characterising the ingredient of the composition
- C08L2207/20—Recycled plastic
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/141—Feedstock
- Y02P20/143—Feedstock the feedstock being recycled material, e.g. plastics
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/62—Plastics recycling; Rubber recycling
Definitions
- the present disclosure relates to a molded article showing visually distinguishable inclusions embedded in a colored plastic matrix and to a thermoplastic polymer composition to obtain it.
- thermoplastic polyolefins are known to have a favorable balance of properties, like high impact resistance and stiffness, lightweight and recyclability, which render thermoplastic polyolefins suitable for use in producing molded items, in particular injection molded articles. Injection molded articles find use in many fields, like in the automotive field.
- molded articles are painted, laminated with films or textile-like materials, or compounded with non-polymeric materials, like non-polymeric fibers.
- US2002/065357A1 discloses a polypropylene molding composition containing up to 3wt.% of carbon fibers, which has a textile-like appearance.
- thermoplastic composition having an appropriate balance of mechanical properties for use in extrusion or injection molding, which can be used for the production of a molded article having a decorative surface.
- the present disclosure provides a colored thermoplastic polymer composition (I) having a lightness value L*, measured in the CIELAB color space, equal to or lower than 40 comprising:
- thermoplastic polymer composition (I) of the instant disclosure is endowed with a good balance of physical-mechanical properties which render the composition suitable for producing preferably, but not exclusively, extruded or injection molded articles having peculiar aesthetic features.
- the present disclosure refers to an article comprising the colored thermoplastic polymer composition (I).
- the article of the instant disclosure is characterized by visually distinguishable inclusions embedded into a colored thermoplastic polymer matrix.
- the present disclosure provides the use of a mica having particle size equal to or lower than 3500 microns, a D50 ranging from 400 to 2500 microns and an aspect ratio equal to or greater than 30 to obtain visually distinguishable inclusions embedded in a colored thermoplastic polymer matrix, the matrix being characterized by a lightness L* value, measured in the CIELAB color space, equal to or lower than 40.
- FIG.l provides a picture of the injection molded test specimen of example El
- FIG.2 provides a picture of the injection molded test specimen of example E2;
- FIG.3 provides a picture of the injection molded test specimen of comparative example
- FIG.4 provides a picture of the injection molded test specimen of comparative example
- the term “consisting essentially of’ means that, in addition to those components which are mandatory, other components may also be present in the material, provided that the essential characteristics of the material are not materially affected by their presence.
- components that, when present in customary amounts, do not materially affect the characteristics of a polymer or of a polyolefin composition, mixture or blend are catalyst residues, processing aids and melt stabilizers;
- copolymer is referred to a polymer deriving from the intentional polymerization of at least two different comonomers, i.e. the term “copolymer” includes terpolymers;
- pre-consumer waste and “post-industrial waste” are synonyms and designate a material diverted from the waste stream originating from a manufacturing process. It might be material trimmings, faulty items, overstock raw materials, excess inventory, etc.; [0030] - the term “post-consumer waste” designate a material that is discarded after it has been used by a final consumer;
- the term “virgin” refers to a polymer obtained from monomers originating from petrochemical feedstock, like natural gas or crude oil, and which has never been used before in a manufacturing process.
- the polyolefin (A) is preferably selected from the group consisting of polypropylene, polyethylene, polystyrene and combinations thereof. More preferably, the thermoplastic polyolefin is blend of polypropylene, polyethylene and polystyrene as described below.
- the polypropylene is preferably selected from the group consisting of:
- HDPE high density polyethylene
- LDPE low density polyethylene
- LLDPE linear low density polyethylene
- elastomeric copolymers of ethylene with from 15.0% to 80.0% by weight, based on the ethylene copolymer, of a comonomer selected from propylene, a CH2 CHR alpha-olefin, wherein R is a linear or branched C2-C8 alkyl group, and combinations thereof.
- the colored thermoplastic composition (I) comprises a blend of an heterophasic propylene polymer and a polyethylene
- the polyethylene and the fraction (b) of the heterophasic propylene polymer are different.
- the alpha-olefin comprised in the ethylene and propylene polymers is preferably independently selected from butene- 1, hexene- 1, octene- 1, 4-methyl-l -pentene and combinations thereof.
- Propylene and ethylene polymers suitable for use as component (A) are known in the art. They can be obtained by polymerizing the relevant monomers in the presence of a Ziegler- Natta or metallocene catalyst system, using known polymerization processes and equipment. Propylene and ethylene polymers are also available on the market, like under the tradename of Hifax and Metocene marketed by LyondellBasell or EngageTM marketed by Dow.
- the polystyrene is preferably a saturated or unsaturated styrene or alpha-methylstyrene block copolymer, preferably comprising up to and including 30% by weight of polymerized styrene, preferably from 5% to 30% by weight, more preferably from 10% to 20% by weight, based on the weight of the polystyrene.
- the polystyrene is a styrene block copolymer selected from the group consisting of: polystyrene-polybutadiene-polystyrene (SBS), polystyrene-poly(ethylene- butylene)-polystyrene (SEBS), polystyrene-poly(ethylene-propylene)-polystyrene (SEPS), polystyrene-polyisoprene-polystyrene (SIS), polystyrene-poly(isoprene-butadiene)-polystyrene (SIBS) and combinations thereof.
- SBS polystyrene-polybutadiene-polystyrene
- SEBS polystyrene-poly(ethylene-butylene)-polystyrene
- SEPS polystyrene-poly(ethylene-propylene)-polystyrene
- Styrene and alpha-methylstyrene block copolymers are preferably prepared by ionic polymerization of the relevant monomers and are commercially available, like under the tradename of KratonTM marketed by Kraton Polymers.
- the polyolefin (A) comprises up to and including 50.0% by weight, preferably from 10.0% to 40.% by weight, more preferably from 15.0% to 35.0% by weight, based on the weight of the polyolefin (A), of a recycled polyolefin, preferably selected from recycled polypropylene, recycled polyethylene, recycles polystyrene and combinations thereof.
- the recycled polyolefin originates from a pre-consumer waste, a post-consumer waste or a combinations thereof, preferably from a post-consumer waste.
- the recycled polyolefin originates from the mechanical recycling of at least one of the above-mentioned waste streams.
- the mechanical recycling processes of post-consumer waste are known in the art and recycled polyolefins are also available on the market.
- the pigment (B) comprised in the colored thermoplastic polymer composition (I) is a dark pigment which, when incorporated into the composition at the claimed concentration provides a colored thermoplastic polymer composition (I) having a lightness value L*, measured in the CIELAB color space, equal to or lower than 40.
- the pigment (B) is organic, inorganic, organo-inorganic or a combination thereof; preferably it is selected from carbon black, oxides of a metal element selected from iron manganese, chromium and mixtures thereof; aniline black and combinations thereof. More preferably, the polymer (B) is carbon black.
- the colored thermoplastic polymer composition (I) comprises from 0.1% to 1.5% by weight, preferably from 0.1% to 1.5% by weight, more preferably from 0.3% to 1.0% by weight of the pigment (B), based on the sum of the weights of (A), (B), (C) and (D).
- the pigment (B) is preferably blended with the other components of the colored thermoplastic polymer composition (I) as concentrated masterbatch, like dispersed in a polymer carrier.
- the colored thermoplastic polymer composition (I) comprises up to and including 10.0% by weight, preferably from 1.0% to 10.0% by weight, more preferably from 2.0% to 8.0% by weight, still preferably from 3.0% to 6.0% by weight, of a mica (C) having particle size equal to or lower than 3500 microns, a D50 ranging from 400 to 2500 microns and an aspect ratio equal to or greater than 30.
- a mica (C) having particle size equal to or lower than 3500 microns, a D50 ranging from 400 to 2500 microns and an aspect ratio equal to or greater than 30.
- the mica (C) has at least one, preferably all, the following properties:
- microns more preferably equal to or lower than 1500 microns; a D50 ranging from 400 to 1500 microns, preferably from 600 to 1300 microns and a D10 equal to or greater than 300 microns, preferably equal to or greater than 400 microns, still preferably equal to or greater than 500 microns; and/or
- the mica (C) is a coated mica, which comprises, still more preferably is coated with, a white inorganic pigment, preferably selected from the group consisting of titanium dioxide, zinc oxide, zinc sulfide and combinations thereof.
- the mica (C) has particle size ranging from 3500 to 1 microns, preferably from 2000 to 50 microns, more preferably from 1700 to 100 microns, still more preferably from 1500 to 200 microns.
- the mica (C) is responsible for the formation of the white inclusions into the dark polymer matrix. If the particle size is greater than 3500 microns, the processing, like extrusion, of the colored thermoplastic polymer composition (I) of the present disclosure is difficult and clogging of the apparatus may occur. If the mica has mean particle size D50, and optionally also D10, outside the ranges described above, an insufficient amount of enclosures (bright/white dots) embedded in the colored thermoplastic matrix can be visually distinguished so that an aesthetic effect is perceived.
- the colored thermoplastic polymer composition (I) comprises from 0.5% to 7.0% by weight, preferably from 1.0% to 5.0% by weight, of an additive (D), wherein the amounts of (D) is based on the total weight of (A), (B), (C ), and (D).
- the additive (D) preferably comprises at least one additive selected from a light stabilizer, like a UV stabilizer, a lubricant and combinations thereof, of the type generally used for plastics.
- the colored thermoplastic polymer composition (I) containing at least one additive (D) has improved scratch resistance with respect to the same composition lacking the additive.
- Further compounds that are preferably comprised in the additive (D) are selected from the group consisting of nucleating agents, antistatic agents, anti-oxidants, slipping agents, lubricants, anti-acids, melt stabilizers, coupling agents and combinations thereof.
- the colored thermoplastic polymer composition (I) further comprises up to and including 40.0% by weight, preferably from 1.0% to 40.0%, more preferably from 5.0% to 30.0% by weight, still preferably from 10.0% to 25.0% by weight, of an inorganic filler (E), wherein the amount (E) is based on the total amount of components (A), (B), (C ), (E) optionally (D).
- the inorganic filler (E) is different from mica and is preferably selected from the group consisting of talc, glass fibers, glass beads, calcium carbonate, wollastonite and combinations thereof, talc being the most preferred.
- the colored thermoplastic polymer composition (I) comprises or consists of:
- thermoplastic polyolefin (A) comprising:
- a propylene polymer fraction (Al) comprising a virgin polypropylene and up to and including 50.0% by weight, preferably from 10.0% to 40.0% by weight, more preferably from 20.0% to 30.0% by weight, of recycled polypropylene (Rl), wherein the amount of the recycled polypropylene (Rl) is based on the weight of the propylene polymer fraction (Al);
- a virgin styrene-block copolymer (A3) comprising up to and including 30% by weight of polymerized styrene, preferably from 5% to 30% by weight, more preferably from 10% to 20% by weight, based on the weight of the polystyrene (A3), wherein the amounts of (Al), (A2) and (A3) are based on total weight of (Al), (A2) and (A3);
- [0066] from 0.1% to 1.5% by weight, preferably from 0.1% to 1.5% by weight, more preferably from 0.3% to 1.0% by weight of a pigment (B) as described above, preferably of carbon black;
- [0067] from 1.0% to 10.0% by weight, preferably from 2.0% to 8.0% by weight, more preferably from 3.0% to 6.0% by weight of a mica (C) as described above;
- polymer additive (D) comprising an additive selected from a light stabilizer, a lubricant or combinations thereof;
- [0069] from 1.0% to 40.0%, more preferably from 5.0% to 30.0% by weight, still preferably from 10.0% to 25.0% by weight, of an inorganic filler (E), preferably talc,
- the virgin polypropylene comprised in the propylene polymer fraction (Al) is preferably selected from the group consisting of virgin propylene homopolymers, virgin heterophasic propylene copolymers and combinations thereof; more preferably the virgin polypropylene is a combination thereof.
- the virgin propylene homopolymer preferably has a melt flow rate greater than 800 g/10 min, preferably ranging from 1,000 to 2,000 g/lOmin, measured according to the method ISO 1133-1 :2011 (230°C/2.16kg).
- the virgin propylene homopolymer comprised in the propylene polymer fraction (Al) is obtained by polymerizing propylene in the presence of any catalyst system suitable to obtain highly stereospecific propylene homopolymers, like a Ziegler Natta catalyst system or a metallocene catalyst, of the type known in the art.
- any catalyst system suitable to obtain highly stereospecific propylene homopolymers like a Ziegler Natta catalyst system or a metallocene catalyst, of the type known in the art.
- the virgin heterophasic propylene copolymer comprised in the propylene polymer fraction (Al) preferably comprises:
- the alpha-olefin comprised in fraction (a) and (b) is preferably independently selected from butene- 1, hexene- 1, octene- 1, 4-methyl-l -pentene and combinations thereof.
- the virgin heterophasic propylene polymer comprised in the propylene polymer fraction (Al) preferably has at least one, preferably all the following properties:
- fraction (a) consists essentially of a propylene homopolymer
- the fraction (a) has solubility in xylene at 25 °C determined according to the method described in the experimental section equal to or lower than 5.0% by weight; and/or [0081] - the comonomer comprised in the fraction (b) is propylene; and/or
- a melt flow rate ranges from 0.5 to 40.0 g/10 min, more preferably from 0.7 to 30.0 g/10 min, measured according to the method ISO 1133-1 :2011 (230°C/2.16kg); and/or
- [0083] - comprises a fraction soluble in xylene at 25°C ranging from 20% to 50% by weight, based on the weight of the heterophasic propylene polymer, wherein the xylene soluble fraction is measured as described in the experimental section;
- the virgin heterophasic propylene polymer comprised in the propylene polymer fraction (Al) is preferably obtained by polymerizing the relevant monomers in the liquid or gasphase in at least two polymerization stages, wherein the second and each subsequent polymerization stage is carried out in the presence of the polymer produced and the catalyst system used in the immediately preceding polymerization stage.
- the polymerization of the relevant monomers is preferably carried out in the presence of a highly stereospecific Ziegler-Natta catalyst systems comprising:
- a solid catalyst component comprising a magnesium halide support on which a Ti compound having at least a Ti-halogen bond is present, and a stereoregulating internal donor;
- the solid catalyst component (1) preferably comprises TiCL in an amount securing the presence of from 0.5 to 10% by weight of Ti with respect to the total weight of the solid catalyst component (1).
- the solid catalyst component (1) comprises at least one stereoregulating internal electron donor compound selected from mono or bidentate organic Lewis bases, preferably selected from esters, ketones, amines, amides, carbamates, carbonates, ethers, nitriles, alkoxysilanes and combinations thereof.
- mono or bidentate organic Lewis bases preferably selected from esters, ketones, amines, amides, carbamates, carbonates, ethers, nitriles, alkoxysilanes and combinations thereof.
- Suitable donors are the esters of phthalic acids such as those described in EP45977A2 and EP395083 A2, in particular di-isobutyl phthalate, di-n- butyl phthalate, di-n-octyl phthalate, diphenyl phthalate, benzylbutyl phthalate and combinations thereof.
- Esters of aliphatic acids can also be selected from esters of malonic acids such as those described in WO98/056830, WO98/056833, WO98/056834, esters of glutaric acids such as those disclosed in WOOO/55215, and esters of succinic acids such as those disclosed WOOO/63261.
- diesters are those deriving from esterification of aliphatic or aromatic diols such as those described in W02010/078494 and USP 7,388,061.
- the internal donor is selected from 1,3-diethers such as those described in EP361493, EP728769 and WO02/100904.
- Preferred magnesium halide support is magnesium dihalide.
- the amount of internal donor that remains fixed on the solid catalyst component (1) is 5 to 20% by moles, with respect to the magnesium dihalide.
- the catalyst system preferably comprises an Al-containing cocatalyst (2) selected from Al-trialkyls, preferably selected from the group consisting of Al-triethyl, Al-triisobutyl and Al-tri- n-butyl.
- the Al/Ti weight ratio in the catalyst system is from 1 to 1000, preferably from 20 to 800.
- the catalyst system comprises a further electron donor compound (3) (external electron donor) selected among silicon compounds, ethers, esters, amines, heterocyclic compounds, particularly 2,2,6,6-tetramethylpiperidine, and ketones.
- Preferred silicon compounds are selected among methylcyclohexyldimethoxysilane (C-donor), dicyclopentyldimethoxysilane (D-donor) and mixtures thereof.
- the polymerization temperature is preferably comprised in the range from 20°C to 100°C and the polymerization pressure is preferably from 3.3 to 4.3 MPa for a process in liquid phase and from 0.5 to 3.0 MPa for a process in the gas phase.
- the molecular weight of the polymers is regulated by feeding a molecular weight regulator, like hydrogen, into a polymerization reactor.
- the amounts of components (a) and (b) correspond to the split between the reactors.
- the recycled propylene polymer (Rl) is preferably a mechanically recycled polypropylene deriving from a pre-consumer waste stream, or a post-consumer waste stream, or a combinations thereof, especially from a post-consumer waste stream, the recycled propylene polymer (Rl) having at least one, preferably all, the following properties:
- melt flow rate ranging from 5.0 to 20.0 g/lOmin, preferably from 8.0 to 17.0 g/lOmin, measured according to the method ISO 1133-1 :2011 (230°C/2.16kg); and/or
- the alpha-olefin is preferably selected from butene- 1, hexene- 1, octene- 1, 4-methyl-l- pentene and combinations thereof.
- the virgin ethylene-alpha olefin elastomer (A2) is different from the fraction (b).
- the ethylene-alpha olefin elastomer (A2) preferably has at least one, more preferably all the following properties:
- melt index ranging from 1.0 to 10.0 g/lOmin, preferably from 3.0 to 8.0 g/lOmin, measured according to the method ISO 1133-1 :2011 (190°C/2.16kg); and/or
- Ethylene copolymers (A2) are commercially available for example under the tradename of Engage, marketed by Dow® and are generally prepared using known polymerization processes, like solution polymerization carried out in the presence of a metallocene-based catalyst system.
- the styrene block copolymer (A3) preferably has at least one, preferably all, the following properties: [0118] - melt index ranging from 5.0 to 50.0 g/10min., preferably from 10.0 to 40.0 g/10min., measured according to the method ASTM D1238 (230°C, 5.0 Kg); and/or
- the colored thermoplastic polymer composition (I) of the present disclosure is prepared by blending the components in an extruder, preferably in a twin-screw extruder, either co-rotating or counter-rotating, operated under conventional conditions, like a temperature above the melting temperature of the thermoplastic polyolefin (A), preferably at a die temperature equal to or greater than 220°C, preferably ranging from 210°to 270°C.
- the process to prepare the colored thermoplastic polymer composition (I) comprises feeding the components to a twin-screw extruder, wherein the mica (C) is fed via a side feeder.
- the colored thermoplastic polymer composition (I) has at least one, preferably all, the following properties:
- melt flow rate equal to or greater than 10.0 g/lOmin, preferably ranging from 15.0 to
- - flexural modulus equal to or greater than 1200 MPa, preferably ranging from 1350
- - impact resistance as measured by the Charpy notched impact according to the method AcN ISO 179/leA, equal to or greater than 30 mJ/mm 2 , preferably ranging from 35 to 50 mJ/mm 2 , at 23°C and equal to or greater than 3.0 mJ/mm 2 , preferably ranging from 3.5 to 7.0 mJ/mm 2 , at -20°C.
- the lightness L* of the colored thermoplastic composition (I) is determined on a portion of the composition wherein no inclusion is embedded.
- the colored thermoplastic polymer composition (I) of the present disclosure are suitable to produce articles having a good balance of physical-mechanical properties and a pleasant aesthetic appearance.
- the present disclosure refers to an article comprising the colored thermoplastic polymer composition (I) described above, characterized in that the article comprises visually distinguishable inclusions embedded in a colored thermoplastic polymer matrix.
- the article is an injection molded article, like an interior or exterior part of a vehicle.
- the article comprises at least 13,000 visually distinguishable inclusions per square meter (acceptable results), more preferably from 14,000 to 20,000 visibly distinguishable inclusions per square meter.
- the visually distinguishable inclusions have a nominal diameter equal to or greater than 150 microns, preferably ranging from 150 to 1,500 microns, wherein the nominal diameter corresponds to the diameter of a circle encompassing the visually distinguishable inclusion.
- the present disclosure refers to the use of a mica having particle size equal to or lower than 3,500 microns, a D50 ranging from 400 to 2500 microns and an aspect ratio equal to or greater than 30 to obtain visually distinguishable inclusions embedded in a colored thermoplastic polymer matrix having a lightness L* value, measured in the CIELAB color space, equal to or lower than 40.
- the mica (c) is preferably endowed with at least one, preferably all, the properties disclosed above.
- thermoplastic polymer is preferably as described above.
- Comonomer content determined by IR using Fourier Transform Infrared Spectrometer (FTIR). The spectrum of a pressed film of the polymer is recorded in absorbance vs. wavenumbers (cm-1). The following measurements are used to calculate the ethylene content:
- the method is calibrated by using polymer standards based on 13C NMR analyses.
- Sample preparation Using a hydraulic press, a thick sheet is obtained by pressing about 1g of sample between two aluminum foils. Pressing temperature is 180 ⁇ 10°C (356°F) and about 10 kg/cm2 pressure for about one minute (minimum two pressing operations for each specimen). A small portion is cut from this sheet to mold a film. Recommended film thickness ranges between 0.02-0.05 cm.
- Flexural Modulus determined according to the method ISO 178:2010 on injection molded test specimens (80 x 10 x 4 mm) obtained according to the method ISO 1873-2:2007.
- Impact resistance Charpy notched impact AcN determined according to the method ISO 179/leA at 23 °C and at -20°C.
- Shrinkage measured on injection molded plaques. 10 test specimen are obtained by injection molding of the thermoplastic composition in a 194,96 x 99,66 x 2,48 mm mold using a Krauss Maffei KM 160 CX injection molding machine (mold temperature 35°C, injection speed 33 mm/s, cooling time 30 min.). The specimens are conditioned for 48h at a temperature of 23 ⁇ 2°C before testing. The dimensions of the specimens are measured with a micrometer and compared to the dimensions of the reference metallic plaque having the same dimensions of the mould. The shrinkage is calculated as mean value over 10 measures using the following formula:
- Ci is the shrinkage in one selected direction (longitudinal or transverse);
- DR is the dimension of the reference metallic plaque in the selected direction
- DS is the dimension of the sample in the selected direction.
- mice [0150] Mica aspect ratio, number of inclusions per m 2 and dimension of the inclusions: visually determined using a digital microscope on an injection molded article.
- PPI a propylene polymer composition consisting essentially of 42% by weight of a fraction (a) comprising a propylene homopolymer and 58% by weight of a fraction (b) comprising propylene-ethylene copolymer containing 42% by weight of units derived from ethylene, the propylene polymer composition having melt flow rate (230°C, 2.16 Kg) of 20.0 g/lOmin and solubility in xylene at 25°C of 35.0% by weight, having flexural modulus greater than 600 MPa.
- the propylene polymer composition PPI is a reactor blend of fraction (a) and fraction (b) obtained by a sequential polymerization in two stages of the relevant monomers.
- PP2 a propylene polymer composition comprising 67% by weight of a fraction (a) comprising a propylene homopolymer, the fraction (a) having solubility in xylene lower than 2.5% by weight and 33% by weight of a fraction (b) comprising a propylene ethylene copolymer containing 33% by weight of units deriving from ethylene, the propylene polymer composition comprising a fraction soluble in xylene of 29.0% by weight and having melt flow rate (230°C, 2.16Kg) of 0.9 g/lOmin and a flexural modulus of 800 MPa.
- the propylene polymer composition PP2 was obtained as described in W02004/087805, example 4.
- PP3 an extremely high melt flow rate propylene homopolymer having melt flow rate (230°C, 2.16 Kg) of 1800 g/lOmin obtained by a metallocene catalyst system.
- rPP mechanically recycled polypropylene having melt flow rate (230°C, 2.16 Kg) of 12.0 g/lOmin, density of 0.90 g/cm3 (ISO1183) and flexural modulus of 1100 MPa.
- EngageTM 11547 an ethylene-octene elastomer marketed by Dow, having melt index (ASTM D1238, 190°C/2.16Kg) of 5.0 g/lOmin, tensile modulus 100% secant (ASTM D638 on compression molded samples) 1.50 MPa and tear strength (ASTM D624) of 22.0 kN/m.
- KratonTM G1657 a linear triblock copolymer based on styrene and ethylene/butylene marketed by Kraton Corp., with a polystyrene content of 13 wt.%, having melt index (230°C, 5.0 Kg) of 22.0 G710 min and a Shore A value (ASTM D2240) of 47.
- Luzenac HAR® talc T84 a talc marketed by Imerys.
- Micacolor 600SF mica marketed by SOPAP (Societe de Production et d’ Adaptation des Polymeres), France. Micacolor 600SF has particle size lower than 1300 microns, D50 of ca.870 microns and D10 of ca. 630 microns.
- Micavi 700 supplied by Cavisa, the mica has particle size lower than 900 microns, D50 of ca.450 microns and D10 of ca. 320 microns.
- Mica-MUTM 800 mica marketed by Imerys having particle size of less than 900 microns, a D50 lower than 300 microns and a D10 lower than 100 microns.
- Chimassorb® 944 light stabilizer marketed by BASF (CAS No. 71878-19-8).
- Tinuvin® 770 bis(2,2,6,6,-tetramethyl-4-piperidyl)sebacate, a light stabilizer marketed by BASF.
- Pigment concentrate masterbatch containing 70 wt.% of carbon black and 50 wt.% of polyolefin carrier.
- thermoplastic polymer compositions were prepared by blending the components indicated in table 1 in a ZSK-70 extruder, operated at a melting temperature ranging from 185°C to 240°C at 200-300 rpm.
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Abstract
Description
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Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| EP22214425 | 2022-12-19 | ||
| PCT/EP2023/085467 WO2024132732A1 (en) | 2022-12-19 | 2023-12-13 | Colored thermoplastic composition |
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| EP4638578A1 true EP4638578A1 (en) | 2025-10-29 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| EP23821672.5A Pending EP4638578A1 (en) | 2022-12-19 | 2023-12-13 | Colored thermoplastic composition |
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| EP (1) | EP4638578A1 (en) |
| JP (1) | JP2025541180A (en) |
| KR (1) | KR20250129692A (en) |
| CN (1) | CN120322497A (en) |
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Family Cites Families (22)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| IT1096661B (en) | 1978-06-13 | 1985-08-26 | Montedison Spa | PROCEDURE FOR THE PREPARATION OF SOLID SPHEROIDAL PRODUCTS AT AMBIENT TEMPERATURE |
| IT1098272B (en) | 1978-08-22 | 1985-09-07 | Montedison Spa | COMPONENTS, CATALYSTS AND CATALYSTS FOR THE POLYMERIZATION OF ALPHA-OLEFINS |
| IT1209255B (en) | 1980-08-13 | 1989-07-16 | Montedison Spa | CATALYSTS FOR THE POLYMERIZATION OF OLEFINE. |
| JPS59135124A (en) * | 1983-01-21 | 1984-08-03 | Kuraray Co Ltd | Preparation of tough thermoplastic resin sheet like article |
| IT1227260B (en) | 1988-09-30 | 1991-03-28 | Himont Inc | DIETTERS THAT CAN BE USED IN THE PREPARATION OF ZIEGLER-NATTA CATALYSTS |
| IT1230134B (en) | 1989-04-28 | 1991-10-14 | Himont Inc | COMPONENTS AND CATALYSTS FOR THE POLYMERIZATION OF OLEFINE. |
| KR930019643A (en) | 1991-06-27 | 1993-10-18 | 크누트 샤우에르테, 클라우스 대너 | 2- (4-substituted phenylhydrazino) -2-thiazoline and 2- (4-substituted phenylazo) -2-thiazoline, methods for their preparation and their use to rescue external parasitic layers |
| DE4332587C2 (en) | 1993-09-24 | 1998-01-15 | Color Plastic Chemie Albert Sc | Fiber-containing plastic, process for its production, use of the plastic for the production of a masterbatch or a polymer compound |
| IL117114A (en) | 1995-02-21 | 2000-02-17 | Montell North America Inc | Components and catalysts for the polymerization ofolefins |
| IL127230A (en) | 1997-03-29 | 2004-07-25 | Montell Technology Company Bv | Magnesium dichloride-alcohol adducts, process for their preparation and catalyst components obtained therefrom |
| IT1292109B1 (en) | 1997-06-09 | 1999-01-25 | Montell North America Inc | COMPONENTS AND CATALYSTS FOR THE POLYMERIZATION OF OLEFINE |
| IT1292108B1 (en) | 1997-06-09 | 1999-01-25 | Montell North America Inc | COMPONENTS AND CATALYSTS FOR THE POLYMERIZATION OF OLEFINE |
| IT1292107B1 (en) | 1997-06-09 | 1999-01-25 | Montell North America Inc | COMPONENTS AND CATALYSTS FOR THE POLYMERIZATION OF OLEFINE |
| KR20010043615A (en) | 1999-03-15 | 2001-05-25 | 바셀 테크놀로지 컴퍼니 비.브이. | Components and catalysts for the polymerization of olefins |
| CA2334743C (en) | 1999-04-15 | 2010-01-12 | Basell Technology Company B.V. | Components and catalysts for the polymerization of olefins |
| BR0205612B1 (en) | 2001-06-13 | 2011-09-06 | solid catalytic component, catalyst and process for the (co) polymerization of olefins. | |
| CN1169845C (en) | 2002-02-07 | 2004-10-06 | 中国石油化工股份有限公司 | Solid catalyst component for olefin polymerization and catalyst containing same and use thereof |
| MY136027A (en) | 2003-04-02 | 2008-07-31 | Basell Poliolefine Spa | Polyolefin masterbatch and composition suitable for injection molding |
| US20080315863A1 (en) | 2005-11-17 | 2008-12-25 | Markus Mornhinweg | Apparatus For the Measurement of a Streaming Potential of a Liquid Containing Solid Matter |
| CN102325808B (en) | 2008-12-31 | 2014-03-12 | 陶氏环球技术有限责任公司 | Procatalyst composition with substituted 1,2-phenylene aromatic diester internal donor and method |
| EP2501727B1 (en) | 2009-11-19 | 2014-05-14 | Basell Poliolefine Italia S.r.l. | Process for the preparation of impact resistant propylene polymer compositions |
| WO2018159433A1 (en) * | 2017-02-28 | 2018-09-07 | 株式会社プライムポリマー | Polypropylene resin composition and molded article |
-
2023
- 2023-12-13 KR KR1020257023505A patent/KR20250129692A/en active Pending
- 2023-12-13 CN CN202380084159.3A patent/CN120322497A/en active Pending
- 2023-12-13 EP EP23821672.5A patent/EP4638578A1/en active Pending
- 2023-12-13 JP JP2025533348A patent/JP2025541180A/en active Pending
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| WO2024132732A1 (en) | 2024-06-27 |
| CN120322497A (en) | 2025-07-15 |
| JP2025541180A (en) | 2025-12-18 |
| KR20250129692A (en) | 2025-08-29 |
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