Patent Application
20240166876
Electric vehicles, such as battery-electric vehicles, plug-in hybrid-electric vehicles, mild hybrid-electric vehicles, or full hybrid-electric vehicles generally have an electric powertrain that contains an electric propulsion source (e.g., battery) and a transmission. High performance polymeric materials are often employed in the electric vehicle for various components, such as in high voltage connectors, power converter housings, battery assembly housings, fluid pumps, inverters, busbars, twisted cables, individual sense lead wires, wire crimps, grommet moldings, quick connectors, tees, interconnects, guide rails, sealing rings (e.g., brushless direct current sealing rings, battery cell sealing rings, etc.), etc. Many of these components are “insert molded” in that they are formed by inserting a member (e.g., metal) into a polymer composition as it is being molded. While this process enables the formation of complex parts, the stark differences in the coefficients of thermal expansion of the different materials can lead to cracking when the part is exposed to changes in temperature. For this reason, various attempts have been made to develop performance polymer compositions with a high degree of thermal shock resistance. Unfortunately, none of the attempts have been able to achieve a sufficiently high degree of thermal shock resistance to allow their use in many EV product applications. Furthermore, to the extent higher thermal shock resistance values can be achieved at all, it is often with a commensurate reduction in insulative properties (e.g., comparative tracking index (“CTI”)). As such, a need currently exists for polymer compositions that can exhibit a high degree of thermal shock resistance and/or insulative properties for use in electric vehicle components.
In accordance with one embodiment of the present invention, a polymer composition is disclosed that comprises 100 parts by weight of at least one polyarylene sulfide and from about 20 to about 120 parts by weight of metal hydroxide particles. The polymer composition exhibits a comparative tracking index of about 210 volts or more at a thickness of 3 mm as determined in accordance with IEC 60112:2003.
Other features and aspects of the present invention are set forth in greater detail below.
A full and enabling disclosure of the present invention, including the best mode thereof to one skilled in the art, is set forth more particularly in the remainder of the specification, including reference to the accompanying figures, in which:
It is to be understood by one of ordinary skill in the art that the present discussion is a description of exemplary embodiments only, and is not intended as limiting the broader aspects of the present invention.
Generally speaking, the present invention is directed to a polymer composition that may contain an impact modifier and metal hydroxide particles dispersed within a polymer matrix that includes at least one polyarylene sulfide. By selectively controlling the particular components and their relative concentration, it has been discovered that the resulting composition may exhibit improved properties for use in forming components of an electric vehicle, such as a battery-powered electric vehicle, fuel cell-powered electric vehicle, plug-in hybrid-electric vehicle (PHEV), mild hybrid-electric vehicle (MHEV), full hybrid-electric vehicle (FHEV), etc. More particularly, the polymer composition may exhibit good insulative properties. The insulative properties of the polymer composition may be characterized by a high comparative tracking index (“CTI”), such as about 210 volts or more, in some embodiments about 220 volts or more, in some embodiments about 250 volts or more, in some embodiments about 300 volts or more, in some embodiments from about 350 volts to about 600 volts, in some embodiments from about 375 to about 500 volts, and in some embodiments, from about 400 volts to about 4750 volts, as determined in accordance with IEC 60112:2003. The insulative properties may be achieved at relatively small thickness values, such as about 4 millimeters or less, in some embodiments about from about 0.2 to about 3.2 millimeters, and in some embodiments, from about 0.4 to about 3.0 millimeters (e.g., 0.8, 1.2, 2.5, or 3 mm).
The polymer composition may also exhibit a thermal shock resistance value of about 300 or more, in some embodiments about 500 or more, in some embodiments about 800 or more, in some embodiments about 1,000 or more, in some embodiments about 1,200 or more, in some embodiments about 1,500 or more, in some embodiments about 1,800 or more, in some embodiments about 2,000 or more, and in some embodiments, about 3,000 or more. As used herein, the “thermal shock resistance value” is determined according to the test described below and generally refers to the number of heating cycles a set of sample components is able to withstand without undergoing visual cracking. Such properties may even be achieved at relatively small thickness values, such as noted above. The polymer composition can also exhibit good flame retardant characteristics as determined according to UL 94 testing as described below. For instance, the polymer composition may achieve at least a V-1 rating, and typically a V-0 rating, for specimens having a thickness of 0.8 millimeters.
While exhibiting good thermal shock resistance, flame retardancy, and high CTI values, the composition may still exhibit good flow properties as reflected by a relatively low melt viscosity, such as about 30 kP or less, in some embodiments about 20 kP or less, in some embodiments about 10 kP or less, in some embodiments about 5 kP or less, and in some embodiments, from about 2 to about 50 kP, as determined in accordance with ISO 11443:2021 at a temperature of about 310° C. and at a shear rate of 400 s−1. Despite having a low melt viscosity, the polymer composition may nevertheless maintain a high degree of impact strength as well as tensile strength, which can provide enhanced flexibility for the resulting component. For example, the polymer composition may exhibit a notched Izod impact strength of about 5 kJ/m2 or more, such as in some embodiments from about 6 to about 50 kJ/m2, and in some embodiments, from about 7 to about 30 kJ/m2, as determined at a temperature of 23° C. in accordance with ISO 180:2019, as well as a Charpy notched impact strength of about 5 kJ/m2 or more, such as in some embodiments from about 6 to about 30 kJ/m2, and in some embodiments, from about 7 to about 20 kJ/m2, as determined at a temperature of 23° C. in accordance with ISO 179-1:2010. For example, the composition may exhibit a tensile stress at break of about 50 MPa or more, in some embodiments from about 80 MPa to about 250 MPa, and in some embodiments, from about 100 to about 200 MPa; a tensile break strain of about 1% or more, in some embodiments from about 1.2% to about 5%; and/or a tensile modulus of about 8,000 MPa or more, in some embodiments from about 9,000 MPa to about 20,000 MPa, in some embodiments from about 10,000 MPa to about 18,000 MPa. The tensile properties may be determined in accordance with ISO 527:2019 at a temperature of 23° C. The composition may also exhibit a flexural strength of about 50 MPa or more, in some embodiments from about 100 to about 350 MPa, and in some embodiments from about 150 to about 300 MPa, and/or a flexural modulus of from about 5,000 to about 20,000, in some embodiments from about 8,000 MPa to about 18,000 MPa, and in some embodiments, from about 10,000 MPa to about 16,000 MPa. The flexural properties may be determined in accordance with ISO 178:2019 at a temperature of 23° C.
Various embodiments of the present invention will now be described in greater detail below.
A. Polyarylene Sulfide
The polymer composition generally contains one or more polyarylene sulfides, typically in an amount of from about 10 wt. % to about 60 wt. %, in some embodiments from about 20 wt. % to about 50 wt. %, in some embodiments from about 25 wt. % to about 45 wt. %, and in some embodiments, from about 30 wt. % to about 40 wt. % of the entire polymer composition. The polyarylene sulfide may be homopolymers or copolymers. For instance, selective combination of dihaloaromatic compounds can result in a polyarylene sulfide copolymer containing not less than two different units. For instance, when p-dichlorobenzene is used in combination with m-dichlorobenzene or 4,4′-dichlorodiphenylsulfone, a polyarylene sulfide copolymer can be formed containing segments having the structure of formula:
The polyarylene sulfide may be linear, semi-linear, branched, or crosslinked. Linear polyarylene sulfides typically contain 80 mol % or more of the repeating unit —(Ar—S)—. Such linear polymers may also include a small amount of a branching unit or a cross-linking unit, but the amount of branching or cross-linking units is typically less than about 1 mol % of the total monomer units of the polyarylene sulfide. A linear polyarylene sulfide polymer may be a random copolymer or a block copolymer containing the above-mentioned repeating unit. Semi-linear polyarylene sulfides may likewise have a cross-linking structure or a branched structure introduced into the polymer a small amount of one or more monomers having three or more reactive functional groups. By way of example, monomer components used in forming a semi-linear polyarylene sulfide can include an amount of polyhaloaromatic compounds having two or more halogen substituents per molecule which can be utilized in preparing branched polymers. Such monomers can be represented by the formula R′Xn, where each X is selected from chlorine, bromine, and iodine, n is an integer of 3 to 6, and R′ is a polyvalent aromatic radical of valence n which can have up to about 4 methyl substituents, the total number of carbon atoms in R′ being within the range of 6 to about 16. Examples of some polyhaloaromatic compounds having more than two halogens substituted per molecule that can be employed in forming a semi-linear polyarylene sulfide include 1,2,3-trichlorobenzene, 1,2,4-trichlorobenzene, 1,3-dichloro-5-bromobenzene, 1,2,4-triiodobenzene, 1,2,3,5-tetrabromobenzene, hexachlorobenzene, 1,3,5-trichloro-2,4,6-trimethylbenzene, 2,2′,4,4′-tetrachlorobiphenyl, 2,2′,5,5′-tetra-iodobiphenyl, 2,2′,6,6′-tetrabromo-3,3′,5,5′-tetramethylbiphenyl, 1,2,3,4-tetrachloronaphthalene, 1,2,4-tribromo-6-methylnaphthalene, etc., and mixtures thereof.
If desired, the polyarylene sulfide can be functionalized. For instance, a disulfide compound containing reactive functional groups (e.g., carboxyl, hydroxyl, amine, etc.) can be reacted with the polyarylene sulfide. Functionalization of the polyarylene sulfide can further provide sites for bonding between any impact modifiers and the polyarylene sulfide, which can improve distribution of the impact modifier throughout the polyarylene sulfide and prevent phase separation. The disulfide compound may undergo a chain scission reaction with the polyarylene sulfide during melt processing to lower its overall melt viscosity. When employed, disulfide compounds typically constitute from about 0.01 wt. % to about 3 wt. %, in some embodiments from about 0.02 wt. % to about 1 wt. %, and in some embodiments, from about 0.05 to about 0.5 wt. % of the polymer composition. The ratio of the amount of the polyarylene sulfide to the amount of the disulfide compound may likewise be from about 1000:1 to about 10:1, from about 500:1 to about 20:1, or from about 400:1 to about 30:1. Suitable disulfide compounds are typically those having the following formula:
R3—S—S—R4
The melt flow rate of a polyarylene sulfide may be from about 100 to about 800 grams per 10 minutes (“g/10 min”), in some embodiments from about 200 to about 700 g/10 min, and in some embodiments, from about 300 to about 600 g/10 min, as determined in accordance with ISO 1133 at a load of 5 kg and temperature of 316° C.
The polyarylene sulfides, such as described above, typically have a DTUL value of from about 70° C. to about 220° C., in some embodiments from about 90° C. to about 200° C., and in some embodiments, from about 120° C. to about 180° C. as determined in accordance with ISO 75-2:2013 at a load of 1.8 MPa. The polyarylene sulfides likewise typically have a glass transition temperature of from about 50° C. to about 120° C., in some embodiments from about 60° C. to about 115° C., and in some embodiments, from about 70° C. to about 110° C., as well as a melting temperature of from about 220° C. to about 340° C., in some embodiments from about 240° C. to about 320° C., and in some embodiments, from about 260° C. to about 300° C.
B. Metal Hydroxide Particles
As noted above, the polymer composition may also contain metal hydroxide particles to help achieve the desired properties. Typically, the particles constitute from about 20 to about 120 parts, in some embodiments from about 25 to about 115 parts, in some embodiments from about 50 to about 115 parts, and in some embodiments, from about 80 to about 110 parts by weight per 100 parts by weight of the polyarylene sulfide(s). For example, the particles may constitute from about 1 wt. % to about 55 wt. %, in some embodiments from about 5 wt. % to about 50 wt. %, in some embodiments from about 8 wt. % to about 35 wt. %, and in some embodiments, from about 15 wt. % to about 45 wt. % of the polymer composition.
The metal hydroxide particles generally contain at least one metal hydroxide having the general formula: M(OH)aOb, where 0≤a≤3 (e.g., 1), b=(3−a)/2, and M is a metal, such magnesium, aluminum, etc. Aluminum hydroxide particles are particularly suitable. In one particular embodiment, for example, the particles exhibit a boehmite crystal phase and the aluminum hydroxide may have the formula AlO(OH) (“aluminum oxide hydroxide”), The metal hydroxide particles may be needle-shaped, elipsoidal-shaped, platelet-shaped, spherical-shaped, etc. Regardless, the particles typically have a median particle diameter (D50) of from about 50 to about 800 nanometers, in some embodiments from about 150 to about 700 nanometers, and in some embodiments, from about 250 to about 500 nanometers, as determined by non-invasive back scatter (NIBS) techniques. If desired, the particles may also have a high specific surface area, such as from about 2 square meters per gram (m2/g) to about 100 m2/g, in some embodiments from about 5 m2/g to about 50 m2/g, and in some embodiments, from about 10 m2/g to about 30 m2/g. Surface area may be determined by the physical gas adsorption (BET) method (nitrogen as the adsorption gas) in accordance with ISO 9277:2010. The moisture content may also be relatively low, such as about 5% or less, in some embodiments about 3% or less, and in some embodiments, from about 0.1 to about 1% as determined in accordance with ISO 787-2:1981.
C. Optional Components
In addition to the components noted above, the polymer composition may also contain a variety of other optional components to help improve its overall properties. In one embodiment, for instance, an impact modifier may be employed within the polymer composition. When employed, the impact modifier(s) may constitute from about 1 to about 30 parts, in some embodiments from about 2 to about 20 parts, and in some embodiments, from about 5 to about 15 parts by weight per 100 parts by weight of the polyarylene sulfide(s). For example, the impact modifiers may constitute from about 0.1 wt. % to about 20 wt. %, in some embodiments from about 0.5 wt. % to about 15 wt. %, and in some embodiments, from about 1 wt. % to about 10 wt. % of the polymer composition.
Examples of suitable impact modifiers may include, for instance, polyepoxides, polyurethanes, polybutadiene, acrylonitrile-butadiene-styrene, polyamides, block copolymers (e.g., polyether-polyamide block copolymers), etc., as well as mixtures thereof. In one embodiment, an olefin copolymer is employed that is “epoxy-functionalized” in that it contains, on average, two or more epoxy functional groups per molecule. The copolymer generally contains an olefinic monomeric unit that is derived from one or more α-olefins. Examples of such monomers include, for instance, linear and/or branched α-olefins having from 2 to 20 carbon atoms and typically from 2 to 8 carbon atoms. Specific examples include ethylene, propylene, 1-butene; 3-methyl-1-butene; 3,3-dimethyl-1-butene; 1-pentene; 1-pentene with one or more methyl, ethyl or propyl substituents; 1-hexene with one or more methyl, ethyl or propyl substituents; 1-heptene with one or more methyl, ethyl or propyl substituents; 1-octene with one or more methyl, ethyl or propyl substituents; 1-nonene with one or more methyl, ethyl or propyl substituents; ethyl, methyl or dimethyl-substituted 1-decene; 1-dodecene; and styrene. Particularly desired α-olefin monomers are ethylene and propylene. The copolymer may also contain an epoxy-functional monomeric unit. One example of such a unit is an epoxy-functional (meth)acrylic monomeric component. As used herein, the term “(meth)acrylic” includes acrylic and methacrylic monomers, as well as salts or esters thereof, such as acrylate and methacrylate monomers. For example, suitable epoxy-functional (meth)acrylic monomers may include, but are not limited to, those containing 1,2-epoxy groups, such as glycidyl acrylate and glycidyl methacrylate. Other suitable epoxy-functional monomers include allyl glycidyl ether, glycidyl ethacrylate, and glycidyl itoconate. Other suitable monomers may also be employed to help achieve the desired molecular weight.
Of course, the copolymer may also contain other monomeric units as is known in the art. For example, another suitable monomer may include a (meth)acrylic monomer that is not epoxy-functional. Examples of such (meth)acrylic monomers may include methyl acrylate, ethyl acrylate, n-propyl acrylate, i-propyl acrylate, n-butyl acrylate, s-butyl acrylate, i-butyl acrylate, t-butyl acrylate, n-amyl acrylate, i-amyl acrylate, isobornyl acrylate, n-hexyl acrylate, 2-ethylbutyl acrylate, 2-ethylhexyl acrylate, n-octyl acrylate, n-decyl acrylate, methylcyclohexyl acrylate, cyclopentyl acrylate, cyclohexyl acrylate, methyl methacrylate, ethyl methacrylate, 2-hydroxyethyl methacrylate, n-propyl methacrylate, n-butyl methacrylate, i-propyl methacrylate, i-butyl methacrylate, n-amyl methacrylate, n-hexyl methacrylate, i-amyl methacrylate, s-butyl-methacrylate, t-butyl methacrylate, 2-ethylbutyl methacrylate, methylcyclohexyl methacrylate, cinnamyl methacrylate, crotyl methacrylate, cyclohexyl methacrylate, cyclopentyl methacrylate, 2-ethoxyethyl methacrylate, isobornyl methacrylate, etc., as well as combinations thereof. In one particular embodiment, for example, the copolymer may be a terpolymer formed from an epoxy-functional (meth)acrylic monomeric component, α-olefin monomeric component, and non-epoxy functional (meth)acrylic monomeric component. The copolymer may, for instance, be poly(ethylene-co-butylacrylate-co-glycidyl methacrylate), which has the following structure:
The relative portion of the monomeric component(s) may be selected to achieve a balance between epoxy-reactivity and melt flow rate. More particularly, high epoxy monomer contents can result in good reactivity with the polyarylene sulfide, but too high of a content may reduce the melt flow rate to such an extent that the copolymer adversely impacts the melt strength of the polymer blend. Thus, in most embodiments, the epoxy-functional (meth)acrylic monomer(s) constitute from about 1 wt. % to about 20 wt. %, in some embodiments from about 2 wt. % to about 15 wt. %, and in some embodiments, from about 3 wt. % to about 10 wt. % of the copolymer. The α-olefin monomer(s) may likewise constitute from about 55 wt. % to about 95 wt. %, in some embodiments from about 60 wt. % to about 90 wt. %, and in some embodiments, from about 65 wt. % to about 85 wt. % of the copolymer. When employed, other monomeric components (e.g., non-epoxy functional (meth)acrylic monomers) may constitute from about 5 wt. % to about 35 wt. %, in some embodiments from about 8 wt. % to about 30 wt. %, and in some embodiments, from about 10 wt. % to about 25 wt. % of the copolymer. The resulting melt flow rate is typically from about 1 to about 30 grams per 10 minutes (“g/10 min”), in some embodiments from about 2 to about 20 g/10 min, and in some embodiments, from about 3 to about 15 g/10 min, as determined in accordance with ASTM D1238-13 at a load of 2.16 kg and temperature of 190° C.
If desired, additional impact modifiers may also be employed in combination with the epoxy-functional impact modifier. For example, the additional impact modifier may include a block copolymer in which at least one phase is made of a material that is hard at room temperature but fluid upon heating and another phase is a softer material that is rubber-like at room temperature. For instance, the block copolymer may have an A-B or A-B-A block copolymer repeating structure, where A represents hard segments and B is a soft segment. Non-limiting examples of impact modifiers having an A-B repeating structure include polyamide/polyether, polysulfone/polydimethylsiloxane, polyurethane/polyester, polyurethane/polyether, polyester/polyether, polycarbonate/polydimethylsiloxane, and polycarbonate/polyether. Triblock copolymers may likewise contain polystyrene as the hard segment and either polybutadiene, polyisoprene, or polyethylene-co-butylene as the soft segment. Similarly, styrene butadiene repeating co-polymers may be employed, as well as polystyrene/polyisoprene repeating polymers. In one particular embodiment, the block copolymer may have alternating blocks of polyamide and polyether. Such materials are commercially available, for example from Atofina under the PEBAX™ trade name. The polyamide blocks may be derived from a copolymer of a diacid component and a diamine component or may be prepared by homopolymerization of a cyclic lactam. The polyether block may be derived from homo- or copolymers of cyclic ethers such as ethylene oxide, propylene oxide, and tetrahydrofuran.
A polyamide may also be employed in the polymer composition. When employed, polyamides typically constitute from about 5 to about 40 parts by weight, in some embodiments from about 10 to about 35 parts by weight, and in some embodiments, from about 15 parts to about 30 parts by weight per 100 parts by weight of the polyarylene sulfide(s). For example, polyamides may constitute from about 0.5 wt. % to about 25 wt. %, in some embodiments from about 1 wt. % to about 20 wt. %, and in some embodiments, from about 2 wt. % to about 15 wt. % of the composition.
Polyamides generally have a CO—NH linkage in the main chain and are obtained by condensation of a diamine and a dicarboxylic acid, by ring opening polymerization of lactam, or self-condensation of an amino carboxylic acid. For example, the polyamide may contain aliphatic repeating units derived from an aliphatic diamine, which typically has from 4 to 14 carbon atoms. Examples of such diamines include linear aliphatic alkylenediamines, such as 1,4-tetramethylenediamine, 1,6-hexanediamine, 1,7-heptanediamine, 1,8-octanediamine, 1,9-nonanediamine, 1,10-decanediamine, 1,11-undecanediamine, 1,12-dodecanediamine, etc.; branched aliphatic alkylenediamines, such as 2-methyl-1,5-pentanediamine, 3-methyl-1,5 pentanediamine, 2,2,4-trimethyl-1,6-hexanediamine, 2,4,4-trimethyl-1,6-hexanediamine, 2,4-dimethyl-1,6-hexanediamine, 2-methyl-1,8-octanediamine, 5-methyl-1,9-nonanediamine, etc.; as well as combinations thereof. Of course, aromatic and/or alicyclic diamines may also be employed. Furthermore, examples of the dicarboxylic acid component may include aromatic dicarboxylic acids (e.g., terephthalic acid, isophthalic acid, 2,6-naphthalenedicarboxylic acid, 2,7-naphthalenedicarboxylic acid, 1,4-naphthalenedicarboxylic acid, 1,4-phenylenedioxy-diacetic acid, 1,3-phenylenedioxy-diacetic acid, diphenic acid, 4,4′-oxydibenzoic acid, diphenylmethane-4,4′-dicarboxylic acid, diphenylsulfone-4,4′-dicarboxylic acid, 4,4′-biphenyldicarboxylic acid, etc.), aliphatic dicarboxylic acids (e.g., adipic acid, sebacic acid, etc.), and so forth. Examples of lactams include pyrrolidone, aminocaproic acid, caprolactam, undecanlactam, lauryl lactam, and so forth. Likewise, examples of amino carboxylic acids include amino fatty acids, which are compounds of the aforementioned lactams that have been ring opened by water.
In certain embodiments, an “aliphatic” polyamide is employed that is formed only from aliphatic monomer units (e.g., diamine and dicarboxylic acid monomer units). Particular examples of such aliphatic polyamides include, for instance, nylon-4 (poly-α-pyrrolidone), nylon-6 (polycaproamide), nylon-11 (polyundecanamide), nylon-12 (polydodecanamide), nylon-46 (polytetramethylene adipamide), nylon-66 (polyhexamethylene adipamide), nylon-610, and nylon-612. Nylon-6 and nylon-66 are particularly suitable. In one particular embodiment, for example, nylon-6 or nylon-66 may be used alone. In other embodiments, blends of nylon-6 and nylon-66 may be employed. When such a blend is employed, the weight ratio of nylon-66 to nylon-6 is typically from 1 to about 2, in some embodiments from about 1.1 to about 1.8, and in some embodiments, from about 1.2 to about 1.6.
Of course, it is also possible to include aromatic monomer units in the polyamide such that it is considered semi-aromatic (contains both aliphatic and aromatic monomer units) or wholly aromatic (contains only aromatic monomer units). For instance, suitable semi-aromatic polyamides may include poly(nonamethylene terephthalamide) (PA9T), poly(nonamethylene terephthalamide/nonamethylene decanediamide) (PA9T/910), poly(nonamethylene terephthalamide/nonamethylene dodecanediamide) (PA9T/912), poly(nonamethylene terephthalamide/11-aminoundecanamide) (PA9T/11), poly(nonamethylene terephthalamide/12-aminododecanamide) (PA9T/12), poly(decamethylene terephthalamide/11-aminoundecanamide) (PA10T/11), poly(decamethylene terephthalamide/12-aminododecanamide) (PA10T/12), poly(decamethylene terephthalamide/decamethylene decanediamide) (PA10T/1010), poly(decamethylene terephthalamide/decamethylene dodecanediamide) (PA10T/1012), poly(decamethylene terephlhalamide/tetramethylene hexanediamide) (PA10T/46), poly(decamethylene terephthalamide/caprolactam) (PA10T/6), poly(decamethylene terephthalamide/hexamethylene hexanediamide) (PA10T/66), poly(dodecamethylene lerephthalamide/dodecamelhylene dodecanediarnide) (PA12T/1212), poly(dodecamethylene terephthalamide/caprolactam) (PA12T/6), poly(dodecamethylene terephthalamide/hexamethylene hexanediamide) (PA12T/66), and so forth.
The polyamide employed in the polymer composition is typically crystalline or semi-crystalline in nature and thus has a measurable melting temperature. The melting temperature may be relatively high such that the composition can provide a substantial degree of heat resistance to a resulting part. For example, the polyamide may have a melting temperature of about 220° C. or more, in some embodiments from about 240° C. to about 325° C., and in some embodiments, from about 250° C. to about 335° C. The polyamide may also have a relatively high glass transition temperature, such as about 30° C. or more, in some embodiments about 40° C. or more, and in some embodiments, from about 45° C. to about 140° C. The glass transition and melting temperatures may be determined as is well known in the art using differential scanning calorimetry (“DSC”), such as determined by ISO Test No. 11357-2:2020 (glass transition) and 11357-3:2018 (melting).
Although by no means required, reinforcing fibers may also be employed in certain embodiments of the present invention. Any of a variety of different types of reinforcing fibers may generally be employed, such as polymer fibers, metal fibers, carbonaceous fibers (e.g., graphite, carbide, etc.), inorganic fibers, etc., as well as combinations thereof. Inorganic fibers may be particularly suitable, such as those that are derived from glass; titanates (e.g., potassium titanate); silicates, such as neosilicates, sorosilicates, inosilicates (e.g., calcium inosilicates, such as wollastonite; calcium magnesium inosilicates, such as tremolite; calcium magnesium iron inosilicates, such as actinolite; magnesium iron inosilicates, such as anthophyllite; etc.), phyllosilicates (e.g., aluminum phyllosilicates, such as palygorskite), tectosilicates, etc.; sulfates, such as calcium sulfates (e.g., dehydrated or anhydrous gypsum); mineral wools (e.g., rock or slag wool); and so forth. Glass fibers may be particularly suitable, such as those formed from E-glass, A-glass, C-glass, D-glass, AR-glass, R-glass, S1-glass, S2-glass, etc., as well as mixtures thereof. If desired, the reinforcing fibers may be provided with a sizing agent or other coating as is known in the art. Regardless of the particular type selected, it is generally desired that the fibers have a relatively low elastic modulus to enhance the processability of the resulting polymer composition. The fibers may, for instance, have a Young's modulus of elasticity of less than about 76 GPa, in some embodiments less than about 75 GPa, and in some embodiments, from about 10 to about 74 GPa, as determined in accordance with ASTM C1557-14.
If desired, at least a portion of the reinforcing fibers may have a relatively flat cross-sectional dimension in that they have an aspect ratio of from about 1.5 to about 10, in some embodiments from about 2 to about 8, and in some embodiments, from about 3 to about 5. The aspect ratio is determined by dividing the cross-sectional width of the fibers (i.e., in the direction of the major axis) by the cross-sectional thickness of the fibers (i.e., in the direction of the minor axis). The shape of such fibers may be in the form of an ellipse, rectangle, rectangle with one or more rounded corners, etc. The cross-sectional width of the fibers may be from about 1 to about 50 micrometers, in some embodiments from about 5 to about 45 micrometers, and in some embodiments, from about 10 to about 35 micrometers. The fibers may also have a thickness of from about 0.5 to about 30 micrometers, in some embodiments from about 1 to about 20 micrometers, and in some embodiments, from about 3 to about 15 micrometers. It should be understood that the cross-sectional thickness and/or width need not be uniform over the entire cross-section. In such circumstances, the cross-sectional width is considered as the largest dimension along the major axis of the fiber and the cross-sectional thickness is considered as the largest dimension along the minor axis. For example, the cross-sectional thickness for an elliptical fiber is the minor diameter of the ellipse.
The reinforcing fibers may also have a narrow size distribution. That is, at least about 60% by volume of the fibers, in some embodiments at least about 70% by volume of the fibers, and in some embodiments, at least about 80% by volume of the fibers may have a width and/or thickness within the ranges noted above. The fibers may be endless or chopped fibers, such as those having a length of from about 1 to about 15 millimeters, and in some embodiments, from about 2 to about 6 millimeters. The dimension of the fibers (e.g., length, width, and thickness) may be determined using known optical microscopy techniques.
When employed, the amount of reinforcing fibers may be selectively controlled to achieve the desired combination of CTI, flow, and mechanical properties. The reinforcing fibers may, for example, be employed in an amount of from about 30 to about 200 parts, in some embodiments from about 35 to about 150 parts, and in some embodiments, from about 40 to about 120 parts per 100 parts by weight of the polyarylene sulfide(s). The reinforcing fibers may, for instance, constitute from about 5 wt. % to about 50 wt. %, in some embodiments from about 10 wt. % to about 40 wt. %, and in some embodiments, from about 15 wt. % to about 35 wt. % of the polymer composition. The relative portion of the reinforcing fibers to the metal hydroxide particles may also be selectively controlled. For example, the weight ratio of the reinforcing fibers to such particles may be from about 0.6 to about 1.8, in some embodiments from about 0.7 to about 1.5, and in some embodiments, from about 0.8 to about 1.2.
In addition to the components noted above, the polymer composition may also contain a variety of other optional components to help improve its overall properties. In one embodiment, for instance, a siloxane polymer may be employed in the polymer composition. Such siloxane polymer(s) typically constitute from about 0.05 to about 10 parts, in some embodiments from about 0.1 to about 5 parts, and in some embodiments, from about 0.4 to about 2 parts by weight per 100 parts by weight of the polyarylene sulfide(s). For example, siloxane polymer(s) may constitute from about 0.01 wt. % to about 5 wt. %, in some embodiments from about 0.05 wt. % to about 4 wt. %, and in some embodiments, from about 0.1 wt. % to about 2 wt. % of the polymer composition. The siloxane polymer generally has a high molecular weight, such as a weight average molecular weight of about 100,000 grams per mole or more, in some embodiments about 200,000 grams per mole or more, and in some embodiments, from about 500,000 grams per mole to about 2,000,000 grams per mole. The siloxane polymer may also have a relatively high kinematic viscosity at 25° C., such as about 10,000 centistokes or more, in some embodiments about 30,000 centistokes or more, and in some embodiments, from about 50,000 to about 50×106 centistokes, such as from about 1×106 to 50×106 centistokes. The viscosity of a siloxane polymer can be determined according to ASTM D445-21.
Any of a variety of high molecular weight siloxane polymers may generally be employed in the polymer composition. A high molecular weight siloxane polymer generally includes siloxane-based monomer residue repeating units. As used herein, “siloxane” denotes a monomer residue repeat unit having the structure:
The silicone may include branch points such as
As used herein, the term “hydrocarbyl” denotes a univalent group formed by removing a hydrogen atom from a hydrocarbon (e.g., alkyl groups, such as ethyl, or aryl groups, such as phenyl). In one or more embodiments, a siloxane monomer residue can be any dialkyl, diaryl, dialkaryl, or diaralkyl siloxane, having the same or differing alkyl, aryl, alkaryl, or aralkyl moieties. In an embodiment, each of R1 and R2 is independently a C1 to C20, C1 to C12, or C1 to C6 alkyl (e.g., methyl, ethyl, propyl, butyl, etc.), aryl (e.g., phenyl), alkaryl, aralkyl, cycloalkyl (e.g., cyclopentyl), arylenyl, alkenyl, cycloalkenyl (e.g., cyclohexenyl), alkoxy (e.g., methoxy), etc., as well as combinations thereof. In various embodiments, R1 and R2 can have the same or a different number of carbon atoms. In various embodiments, the hydrocarbyl group for each of R1 and R2 is an alkyl group that is saturated and optionally straight-chain. Additionally, the alkyl group in such embodiments can be the same for each of R1 and R2 of a polymer chain. Non-limiting examples of alkyl groups suitable for use in R1 and R2 include methyl, ethyl 1-propyl, 2-propyl, 1-butyl, isobutyl, t-butyl, or combinations of two or more thereof.
Additionally, the siloxane polymer can contain various terminating groups as an R1 and/or R2 group, such as vinyl groups, hydroxyl groups, hydrides, isocyanate groups, epoxy groups, acid groups, halogen atoms, alkoxy groups, acyloxy groups, ketoximate groups, amino groups, amido groups, acid amido groups, amino-oxy groups, mercapto groups, alkenyloxy groups, alkoxyalkoxy groups, or aminoxy groups as well as combinations thereof, Additionally, a polymer composition can include a mixture of two or more siloxane polymers.
In some embodiments, a high molecular weight siloxane polymer can be proved by copolymerizing multiple siloxane polymers having a low weight average molecular weight (e.g., a molecular weight of less than 100,000 grams per mole) with polysiloxane linkers. In one particular embodiment, for instance, the resin may be formed by copolymerizing one or more low molecular siloxane polymer(s) with a linear polydiorganosiloxane linker, such as described in U.S. Pat. No. 6,072,012 to Juen, et al. A substantially linear polydiorganosiloxane linker may have the following general formula:
(R3(3-p)R4pSiO1/2)(R32SiO2/2)x((R3R4SiO2/2)(R32SiO2/2)x)y(R3(3-p)R4pSiO1/2)
In certain embodiments, the siloxane polymer may be provided in the form of a masterbatch that includes a carrier resin. The carrier resin may, for instance, constitute from about 0.05 wt. % to about 15 wt. %, in some embodiments from about 0.1 wt. % to about 10 wt. %, and in some embodiments, from about 0.5 wt. % to about 8 wt. % of the polymer composition. Any of a variety of carrier resins may be employed, such as polyolefins (ethylene polymer, propylene polymers, etc.), polyamides, etc. In one embodiment, for example, the carrier resin is an ethylene polymer. The ethylene polymer may be a copolymer of ethylene and an α-olefin, such as a C3-C20 α-olefin or C3-C12 α-olefin. Suitable α-olefins may be linear or branched (e.g., one or more C1-C3 alkyl branches, or an aryl group). Specific examples include 1-butene; 3-methyl-1-butene; 3,3-dimethyl-1-butene; 1-pentene; 1-pentene with one or more methyl, ethyl or propyl substituents; 1-hexene with one or more methyl, ethyl or propyl substituents; 1-heptene with one or more methyl, ethyl or propyl substituents; 1-octene with one or more methyl, ethyl or propyl substituents; 1-nonene with one or more methyl, ethyl or propyl substituents; ethyl, methyl or dimethyl-substituted 1-decene; 1-dodecene; and styrene. Particularly desired α-olefin comonomers are 1-butene, 1-hexene and 1-octene. The ethylene content of such copolymers may be from about 60 mole % to about 99 mole %, in some embodiments from about 80 mole % to about 98.5 mole %, and in some embodiments, from about 87 mole % to about 97.5 mole %. The α-olefin content may likewise range from about 1 mole % to about 40 mole %, in some embodiments from about 1.5 mole % to about 15 mole %, and in some embodiments, from about 2.5 mole % to about 13 mole %. The density of the ethylene polymer may vary depending on the type of polymer employed, but generally ranges from about 0.85 to about 0.96 grams per cubic centimeter (g/cm3). Polyethylene “plastomers”, for instance, may have a density in the range of from about 0.85 to about 0.91 g/cm3. Likewise, “linear low density polyethylene” (LLDPE) may have a density in the range of from about 0.91 to about 0.940 g/cm3; “low density polyethylene” (LDPE) may have a density in the range of from about 0.910 to about 0.940 g/cm3; and “high density polyethylene” (HDPE) may have density in the range of from about 0.940 to about 0.960 g/cm3, such as determined in accordance with ASTM D792. Some non-limiting examples of high molecular weight siloxane polymer masterbatches that may be employed include, for instance, those available from Dow Corning under the trade designations MB50-001, MB50-002, MB50-313, MB50-314 and MB50-321.
If desired, an organosilane compound may also be employed in the polymer composition, such as in an amount of from about 0.1 to about 8 parts, in some embodiments from about 0.3 to about 5 parts, and in some embodiments, from about 0.5 to about 3 parts by weight per 100 parts by weight of the polyarylene sulfide(s). For example, organosilane compounds can constitute from about 0.01 wt. % to about 3 wt. %, in some embodiments from about 0.02 wt. % to about 2 wt. %, and in some embodiments, from about 0.05 to about 1 wt. % of the polymer composition. The organosilane compound may, for example, be any alkoxysilane as is known in the art, such as vinlyalkoxysilanes, epoxyalkoxysilanes, aminoalkoxysilanes, mercaptoalkoxysilanes, and combinations thereof. In one embodiment, for instance, the organosilane compound may have the following general formula:
R5—Si—(R6)3,
Some representative examples of organosilane compounds that may be included in the mixture include mercaptopropyl trimethyoxysilane, mercaptopropyl triethoxysilane, aminopropyl triethoxysilane, aminoethyl triethoxysilane, aminopropyl trimethoxysilane, aminoethyl trimethoxysilane, ethylene trimethoxysilane, ethylene triethoxysilane, ethyne trimethoxysilane, ethyne triethoxysilane, aminoethylaminopropyltrimethoxysilane, 3-aminopropyl triethoxysilane, 3-aminopropyl trimethoxysilane, 3-aminopropyl methyl dimethoxysilane or 3-aminopropyl methyl diethoxysilane, N-(2-aminoethyl)-3-aminopropyl trimethoxysilane, N-methyl-3-aminopropyl trimethoxysilane, N-phenyl-3-aminopropyl trimethoxysilane, bis(3-aminopropyl) tetramethoxysilane, bis(3-aminopropyl) tetraethoxy disiloxane, γ-aminopropyltrimethoxysilane, γ-aminopropyltriethoxysilane, γ-aminopropylmethyldimethoxysilane, γ-aminopropylmethyldiethoxysilane, N-(β-aminoethyl)-γ-aminopropyltrimethoxysilane, N-phenyl-γ-aminopropyltrimethoxysilane, γ-diallylaminopropyltrimethoxysilane, γ-diallylaminopropyltrimethoxysilane, etc., as well as combinations thereof. Particularly suitable organosilane compounds are 3-aminopropyltriethoxysilane and 3-mercaptopropyltrimethoxysilane.
The polymer composition may also contain a heat stabilizer. By way of example, the heat stabilizer can be a phosphite stabilizer, such as an organic phosphite. For example, suitable phosphite stabilizers include monophosphites and diphosphites, wherein the diphosphite has a molecular configuration that inhibits the absorption of moisture and/or has a relatively high Spiro isomer content. For instance, a diphosphite stabilizer may be selected that has a spiro isomer content of greater than 90%, such as greater than 95%, such as greater than 98%. Specific examples of such diphosphite stabilizers include, for instance, bis(2,4-dicumylphenyl)pentaerythritol diphosphite, bis(2,4-di-t-butylphenyl)pentaerythritol diphosphite, distearyl pentaerythritol diphosphite, mixtures thereof, etc. When employed, heat stabilizers typically constitute from about 0.1 wt. % to about 3 wt. %, and in some embodiments, from about 0.2 wt. % to about 2 wt. % of the composition.
If desired, a crosslinking system may also be employed to help further improve the strength and flexibility of the composition under a variety of different conditions. In such circumstances, a crosslinked product may be formed from a crosslinkable polymer composition that contains the polyarylene sulfide(s), in conjunction with one or more optional impact modifiers. When employed, such a crosslinking system, which may contain one or more crosslinking agents, typically constitutes from about 0.1 to about 15 parts, in some embodiments from about 0.2 to about 10 parts, and in some embodiments, from about 0.5 to about 5 parts per 100 parts by weight of the polyarylene sulfide(s), as well as from about 0.05 wt. % to about 15 wt. %, in some embodiments from about 0.1 wt. % to about 10 wt. %, and in some embodiments, from about 0.2 wt. % to about 5 wt. % of the polymer composition. Through the use of such a crosslinking system, the compatibility and distribution of the polyarylene sulfide and impact modifier can be significantly improved. For example, the impact modifier is capable of being dispersed within the polymer composition in the form of discrete domains of a nano-scale size. For example, the domains may have an average cross-sectional dimension of from about 1 to about 1000 nanometers, in some embodiments from about 5 to about 800 nanometers, in some embodiments from about 10 to about 500 nanometers. The domains may have a variety of different shapes, such as elliptical, spherical, cylindrical, plate-like, tubular, etc. Such improved dispersion can result in either better mechanical properties or allow for equivalent mechanical properties to be achieved at lower amounts of impact modifier.
Any of a variety of different crosslinking agents may generally be employed within the crosslinking system. In one embodiment, for instance, the crosslinking system may include a metal carboxylate. Without intending to be limited by theory, it is believed that the metal atom in the carboxylate can act as a Lewis acid that accepts electrons from the oxygen atom located in a functional group (e.g., epoxy functional group) of the impact modifier. Once it reacts with the carboxylate, the functional group can become activated and can be readily attacked at either carbon atom in the three-membered ring via nucleophilic substitution, thereby resulting in crosslinking between the chains of the impact modifier. The metal carboxylate is typically a metal salt of a fatty acid. The metal cation employed in the salt may vary, but is typically a divalent metal, such as calcium, magnesium, lead, barium, strontium, zinc, iron, cadmium, nickel, copper, tin, etc., as well as mixtures thereof. Zinc is particularly suitable. The fatty acid may generally be any saturated or unsaturated acid having a carbon chain length of from about 8 to 22 carbon atoms, and in some embodiments, from about 10 to about 18 carbon atoms. If desired, the acid may be substituted. Suitable fatty acids may include, for instance, lauric acid, myristic acid, behenic acid, oleic acid, palmitic acid, stearic acid, ricinoleic acid, capric acid, neodecanoic acid, hydrogenated tallow fatty acid, hydroxy stearic acid, the fatty acids of hydrogenated castor oil, erucic acid, coconut oil fatty acid, etc., as well as mixtures thereof. Metal carboxylates typically constitute from about 0.05 wt. % to about 5 wt. %, in some embodiments from about 0.1 wt. % to about 2 wt. %, and in some embodiments, from about 0.2 wt. % to about 1 wt. % of the polymer composition.
The crosslinking system may also employ a crosslinking agent that is “multi-functional” to the extent that it contains at least two reactive, functional groups. Such a multi-functional crosslinking reagent may serve as a weak nucleophile, which can react with activated functional groups on the impact modifier (e.g., epoxy functional groups). The multi-functional nature of such molecules enables them to bridge two functional groups on the impact modifier, effectively serving as a curing agent. The multi-functional crosslinking agents generally include two or more reactively functional terminal moieties linked by a bond or a non-polymeric (non-repeating) linking component. By way of example, the crosslinking agent can include a di-epoxide, poly-functional epoxide, diisocyanate, polyisocyanate, polyhydric alcohol, water-soluble carbodiimide, diamine, diol, diaminoalkane, multi-functional carboxylic acid, diacid halide, etc. Multi-functional carboxylic acids and amines are particularly suitable. Specific examples of multi-functional carboxylic acid crosslinking agents can include, without limitation, isophthalic acid, terephthalic acid, phthalic acid, 1,2-di(p-carboxyphenyl)ethane, 4,4′-dicarboxydiphenyl ether, 4,4′-bisbenzoic acid, 1,4- or 1,5-naphthalene dicarboxylic acids, decahydronaphthalene dicarboxylic acids, norbornene dicarboxylic acids, bicyclooctane dicarboxylic acids, 1,4-cyclohexanedicarboxylic acid (both cis and trans), 1,4-hexylenedicarboxylic acid, adipic acid, azelaic acid, dicarboxyl dodecanoic acid, succinic acid, maleic acid, glutaric acid, suberic acid, azelaic acid and sebacic acid. The corresponding dicarboxylic acid derivatives, such as carboxylic acid diesters having from 1 to 4 carbon atoms in the alcohol radical, carboxylic acid anhydrides or carboxylic acid halides may also be utilized. In certain embodiments, aromatic dicarboxylic acids are particularly suitable, such as isophthalic acid or terephthalic acid.
When employed, multi-functional crosslinking agents typically constitute from about 50 wt. % to about 95 wt. %, in some embodiments from about 60 wt. % to about 90 wt. %, and in some embodiments, from about 70 wt. % to about 85 wt. % of the crosslinking system, while the metal carboxylates typically constitute from about 5 wt. % to about 50 wt. %, in some embodiments from about 10 wt. % to about 40 wt. %, and in some embodiments, from about 15 wt. % to about 30 wt. % of the crosslinking system. For example, the multi-functional crosslinking agents may constitute from about 0.1 wt. % to about 10 wt. %, in some embodiments from about 0.2 wt. % to about 5 wt. %, and in some embodiments, from about 0.5 wt. % to about 3 wt. % of the polymer composition. Of course, in certain embodiments, the composition may be generally free of multi-functional crosslinking agents, or the crosslinking system may be generally free of metal carboxylates.
Still other components that can be included in the composition may include, for instance, particulate fillers (e.g., talc, mica, etc.), antimicrobials, pigments (e.g., black pigments), antioxidants, stabilizers, surfactants, waxes, flow promoters, solid solvents, and other materials added to enhance properties and processability.
The manner in which the polyarylene sulfide(s), metal hydroxide particles, and various other optional additives are combined may vary as is known in the art. For instance, the materials may be supplied either simultaneously or in sequence to a melt processing device that dispersively blends the materials. Batch and/or continuous melt processing techniques may be employed. For example, a mixer/kneader, Banbury mixer, Farrel continuous mixer, single-screw extruder, twin-screw extruder, roll mill, etc., may be utilized to blend and melt process the materials. One particularly suitable melt processing device is a co-rotating, twin-screw extruder (e.g., Leistritz co-rotating fully intermeshing twin screw extruder). Such extruders may include feeding and venting ports and provide high intensity distributive and dispersive mixing. For example, the components may be fed to the same or different feeding ports of a twin-screw extruder and melt blended to form a substantially homogeneous melted mixture. Melt blending may occur under high shear/pressure and heat to ensure sufficient dispersion. For example, melt processing may occur at a temperature of from about 100° C. to about 500° C., and in some embodiments, from about 150° C. to about 300° C. Likewise, the apparent shear rate during melt processing may range from about 100 seconds−1 to about 10,000 seconds−1, and in some embodiments, from about 500 seconds−1 to about 1,500 seconds−1. Of course, other variables, such as the residence time during melt processing, which is inversely proportional to throughput rate, may also be controlled to achieve the desired degree of homogeneity.
If desired, one or more distributive and/or dispersive mixing elements may be employed within the mixing section of the melt processing unit. Suitable distributive mixers may include, for instance, Saxon, Dulmage, Cavity Transfer mixers, etc. Likewise, suitable dispersive mixers may include Blister ring, Leroy/Maddock, CRD mixers, etc. As is well known in the art, the mixing may be further increased in aggressiveness by using pins in the barrel that create a folding and reorientation of the polymer melt, such as those used in Buss Kneader extruders, Cavity Transfer mixers, and Vortex Intermeshing Pin mixers. The speed of the screw can also be controlled to improve the characteristics of the composition. For instance, the screw speed can be about 400 rpm or less, in one embodiment, such as between about 200 rpm and about 350 rpm, or between about 225 rpm and about 325 rpm. In one embodiment, the compounding conditions can be balanced so as to provide a polymer composition that exhibits improved properties. For example, the compounding conditions can include a screw design to provide mild, medium, or aggressive screw conditions. For example, system can have a mildly aggressive screw design in which the screw has one single melting section on the downstream half of the screw aimed towards gentle melting and distributive melt homogenization. A medium aggressive screw design can have a stronger melting section upstream from the filler feed barrel focused more on stronger dispersive elements to achieve uniform melting. Additionally, it can have another gentle mixing section downstream to mix the fillers. This section, although weaker, can still add to the shear intensity of the screw to make it stronger overall than the mildly aggressive design. A highly aggressive screw design can have the strongest shear intensity of the three. The main melting section can be composed of a long array of highly dispersive kneading blocks. The downstream mixing section can utilize a mix of distributive and intensive dispersive elements to achieve uniform dispersion of all type of fillers. The shear intensity of the highly aggressive screw design can be significantly higher than the other two designs. In one embodiment, a system can include a medium to aggressive screw design with relatively mild screw speeds (e.g., between about 200 rpm and about 300 rpm).
The crystallization temperature of the resulting polymer composition (prior to being formed into a shaped part) may be about 250° C. or less, in some embodiments from about 100° C. to about 245° C., and in some embodiments, from about 150° C. to about 240° C. The melting temperature of the polymer composition may also range from 140° C. to about 380° C., in some embodiments from about 200° C. to about 360° C., in some embodiments from about 250° C. to about 320° C., and in some embodiments, from about 260° C. to about 300° C. The melting and crystallization temperatures may be determined as is well known in the art using differential scanning calorimetry in accordance with ISO 11357-3:2018.
A shaped part may be formed from the polymer composition using a variety of different techniques. Suitable techniques may include, for instance, injection molding, low-pressure injection molding, extrusion compression molding, gas injection molding, foam injection molding, low-pressure gas injection molding, low-pressure foam injection molding, gas extrusion compression molding, foam extrusion compression molding, extrusion molding, foam extrusion molding, compression molding, foam compression molding, gas compression molding, etc. For example, an injection molding system may be employed that includes a mold within which the polymer composition may be injected. The time inside the injector may be controlled and optimized so that polymer matrix is not pre-solidified. When the cycle time is reached and the barrel is full for discharge, a piston may be used to inject the composition to the mold cavity. Compression molding systems may also be employed. As with injection molding, the shaping of the polymer composition into the desired article also occurs within a mold. The composition may be placed into the compression mold using any known technique, such as by being picked up by an automated robot arm. The temperature of the mold may be maintained at or above the solidification temperature of the polymer composition for a desired time period to allow for solidification. The molded product may then be solidified by bringing it to a temperature below that of the melting temperature. The resulting product may be de-molded. The cycle time for each molding process may be adjusted to suit the polymer composition, to achieve sufficient bonding, and to enhance overall process productivity.
As indicated above, the unique properties of the polymer composition can more readily allow it to be integrally formed with a metal component having a vastly different thermal coefficient of expansion. Thus, if desired, the polymer composition may be employed in a composite structure that contains a metal component that is integrally formed and in contact with a resinous component that includes the polymer composition of the present invention. This may be accomplished using a variety of techniques, such as by an insert molding process in which the polymer composition is molded (e.g., injection molded) onto a portion or the entire surface of the metal component. The metal component may contain any of a variety of different metals, such as aluminum, stainless steel, magnesium, nickel, chromium, copper, titanium, and alloys thereof. Due to its unique properties, the polymer composition can adhere to the metal component by flowing within and/or around surface indentations or pores of the metal component. To improve adhesion, the metal component may optionally be pretreated to increase the degree of surface indentations and surface area. This may be accomplished using mechanical techniques (e.g., sandblasting, grinding, flaring, punching, molding, etc.) and/or chemical techniques (e.g., etching, anodic oxidation, etc.). In addition to pretreating the surface, the metal component may also be preheated at a temperature close to, but below the melt temperature of the polymer composition. This may be accomplished using a variety of techniques, such as contact heating, radiant gas heating, infrared heating, convection or forced convection air heating, induction heating, microwave heating or combinations thereof. In any event, the polymer composition is generally injected into a mold that contains the optionally preheated metal component.
As previously mentioned, the polymer composition, shaped part, and/or composite structure are particularly beneficial for use in components of an electric vehicle. Referring to
The powertrain 110 may also contain at least one power electronics module 126 that is connected to the battery assembly 124 (also commonly referred to as a battery pack) and that may contain a power converter (e.g., converter, etc., as well as combinations thereof). The power electronics module 126 is typically electrically connected to the electric machines 114 and provides the ability to bi-directionally transfer electrical energy between the battery assembly 124 and the electric machines 114. For example, the battery assembly 124 may provide a DC voltage while the electric machines 114 may require a three-phase AC voltage to function. The power electronics module 126 may convert the DC voltage to a three-phase AC voltage as required by the electric machines 114. In a regenerative mode, the power electronics module 126 may convert the three-phase AC voltage from the electric machines 114 acting as generators to the DC voltage required by the battery assembly 124. The battery assembly 124 may also provide energy for other vehicle electrical systems. For example, the powertrain may employ a DC/DC converter module 128 that converts the high voltage DC output from the battery assembly 124 to a low voltage DC supply that is compatible with other vehicle loads, such as compressors and electric heaters. In a typical vehicle, the low-voltage systems are electrically connected to an auxiliary battery 130 (e.g., 12V battery). A battery energy control module (BECM) 133 may also be present that is in communication with the battery assembly 124 that acts as a controller for the battery assembly 124 and may include an electronic monitoring system that manages temperature and charge state of each of the battery cells. The battery assembly 124 may also have a temperature sensor 131, such as a thermistor or other temperature gauge. The temperature sensor 131 may be in communication with the BECM 133 to provide temperature data regarding the battery assembly 124. The temperature sensor 131 may also be located on or near the battery cells within the traction battery 124. It is also contemplated that more than one temperature sensor 131 may be used to monitor temperature of the battery cells.
In certain embodiments, the battery assembly 124 may be recharged by an external power source 136, such as an electrical outlet. The external power source 136 may be electrically connected to electric vehicle supply equipment (EVSE) that regulates and manages the transfer of electrical energy between the power source 36 and the vehicle 112. The EVSE 138 may have a charge connector 140 for plugging into a charge port 134 of the vehicle 112. The charge port 134 may be any type of port configured to transfer power from the EVSE 138 to the vehicle 112 and may be electrically connected to a charger or on-board power conversion module 132. The power conversion module 132 may condition the power supplied from the EVSE 138 to provide the proper voltage and current levels to the battery assembly 124. The power conversion module 132 may interface with the EVSE 138 to coordinate the delivery of power to the vehicle 112.
The polymer composition described herein can be included in various components of an electric vehicle as illustrated in
The manner in which a busbar connects to individual battery cells of a battery assembly 124, such as shown in
Of course, a busbar may be provided in any suitable shape and size. For instance, a busbar may be used as a template for placing the individual battery cells so that they are uniform in each battery assembly manufactured. In such an embodiment, a busbar may hold individual batteries of a battery assembly 124 in place during the manufacturing process and thermal padding or injection-housings, which can be formed of a polymer composition as described herein, can be added without causing the individual battery cells to shift out of position.
Apart from busbars, other components may also employ the polymer composition of the present invention. For instance,
Another component of an electric vehicle as may incorporate the polymer compositions as described is an inverter system, one exemplary embodiment of which is illustrated in
An inverter system can include several components that can incorporate a polymer composition as disclosed including, without limitation, the EMI filter apparatus 325, e.g., as a housing and/or internal support structures, an EMI filter card 340, the bus bars 310, as well as connectors employed within the system. For example, an electrical connector that includes the polymer composition as described herein may be employed in an inverter system as in
Referring to
Although by no means required, the first connector portion 202 may also include an identification mark 210 secured to or defined by the first protective member 212. The second connecting portion 204 may also optionally define an alignment window 220 sized according to the identification mark 210 to more easily determine when the portions are fully mated. For instance, the identification mark 210 may not be readable unless blockers 221 cover a portion of the identification mark 210. Optionally, the second connecting portion 204 may include a supplemental mark 224 located adjacent to the alignment window 220.
Systems that can employ the polymer composition of the present invention are in no way limited to only electrical systems. For example, a thermal management system can also beneficially incorporate the polymer composition. A thermal management system of an electric vehicle can generally include multiple different subsystems such as, without limitation, a power train subsystem, a refrigeration subsystem, a battery cooling subsystem, and a heating, ventilation, and cooling (HVAC) subsystem. In some embodiments, one or more subsystems of a thermal management system may in fluid communication with one another, thus allowing hot heat transfer medium to flow from the high temperature circuit into the low temperature circuit, and cooler heat transfer medium to flow from the low temperature circuit into the high temperature circuit.
By way of example,
One example of a component of a heat management system as may incorporate the polymer composition of the invention is a coolant pump, e.g., an electric water pump, an example of which is illustrated in
The present invention may be better understood with reference to the following examples.
Melt Viscosity: The melt viscosity (Pa-s) may be determined in accordance with ISO 11443:2021 at a shear rate of 400 s−1 and using a Dynisco LCR7001 capillary rheometer. The rheometer orifice (die) may have a diameter of 1 mm, length of 20 mm, L/D ratio of 20.1, and an entrance angle of 180°. The diameter of the barrel may be 9.55 mm+0.005 mm and the length of the rod was 233.4 mm. The melt viscosity is typically determined at a temperature of 310° C.
Tensile Modulus, Tensile Stress at Break, and Tensile strain at Break: Tensile properties may be tested according to ISO 527-2/1A:2019 (technically equivalent to ASTM D638-14). Modulus and strength measurements may be made on the same test strip sample having a length of 80 mm, thickness of 10 mm, and width of 4 mm. The testing temperature may be 23° C., and the testing speeds may be 5 mm/min.
Flexural Modulus and Flexural Stress: Flexural properties may be tested according to ISO 178:2019 (technically equivalent to ASTM D790-10). This test may be performed on a 64 mm support span. Tests may be run on the center portions of uncut ISO 3167 multi-purpose bars. The testing temperature may be 23° C. and the testing speed may be 2 mm/min.
Izod notched impact strength may be determined according to ISO 180:2019. Specimens were cut from the center of a multi-purpose bar using a single tooth milling machine. Testing temperature was 23° C.
Notched Charpy Impact Strength: Charpy properties may be tested according to ISO Test No. ISO 179-1:2010) (technically equivalent to ASTM D256-10, Method B). This test may be run using a Type 1 specimen size (length of 80 mm, width of 10 mm, and thickness of 4 mm). When testing the notched impact strength, the notch may be a Type A notch (0.25 mm base radius). Specimens may be cut from the center of a multi-purpose bar using a single tooth milling machine. The testing temperature may be 23° C. or −30° C.
Comparative Tracking Index (“CTI”): The comparative tracking index (CTI) may be determined in accordance with International Standard IEC 60112-2003 to provide a quantitative indication of the ability of a composition to perform as an electrical insulating material under wet and/or contaminated conditions. In determining the CTI rating of a composition, two electrodes are placed on a molded test specimen. A voltage differential is then established between the electrodes while a 0.1% aqueous ammonium chloride solution is dropped onto a test specimen. The maximum voltage at which five (5) specimens withstand the test period for 50 drops without failure is determined. The test voltages range from 100 to 600 V in 25 V increments. The numerical value of the voltage that causes failure with the application of fifty (50) drops of the electrolyte is the “comparative tracking index.” The value provides an indication of the relative track resistance of the material. According to UL746A, a nominal part thickness of 3 mm is considered representative of performance at other thicknesses.
Flame Retardancy: The flame retarding efficacy may be determined according to the UL 94 Vertical Burn Test procedure of the “Test for Flammability of Plastic Materials for Parts in Devices and Appliances”, 5th Edition, Oct. 29, 1996. The ratings according to the UL 94 test are listed in the following table:
The “afterflame time” is an average value determined by dividing the total afterflame time (an aggregate value of all samples tested) by the number of samples. The total afterflame time is the sum of the time (in seconds) that all the samples remained ignited after two separate applications of a flame as described in the UL-94 VTM test. Shorter time periods indicate better flame resistance, i.e., the flame went out faster. For a V-0 rating, the total afterflame time for five (5) samples, each having two applications of flame, must not exceed 50 seconds.
Thermal Shock Resistance: To test thermal shock resistance, four (4) types of sample components are initially formed using the molds and inserts shown in
Referring to
A set of twenty (20) sample components may be formed using each of the molds described above. The sample components may then be subjected to a first heating cycle within a thermal shock chamber having a hot zone and a cold zone, such as those commercially available under the name “ShockEvent T/120/V2” from Weisstechnik. The hot zone may be heated to a temperature of 140° C. and the cold zone may be cooled to a temperature of −40° C. To initiate the first heating cycle, the sample components are placed within the hot zone for 30 minutes and then a product carrier within the chamber moves the sample components from the hot zone to the cold zone for an additional 30 minutes. In this manner, the total time of the first cycle is 1 hour. 24 cycles are conducted each day and 1 hour for each cycle. During the first two weeks, the sample components are visually observed for cracking once a day, and thereafter, the sample components are visually observed for cracking twice per week until all twenty (20) samples crack or a full set of cycles is achieved, which may be either 1,500 or 3,000 cycles depending on the testing protocol. When the first sample cracks, the number of cycles achieved prior to cracking is recorded as the “thermal shock resistance value.” If a full set of cycles (1,500 or 3,000) is achieved without all samples cracking, the “thermal shock resistance value” is simply recorded as “>1,500” or “>3,000”, depending on the particular testing protocol.
Examples 1-4 were melt mixed using a 32 mm Coperion co-rotating, fully-intermeshing, twin-screw extruder and include various concentrations of a polyarylene sulfide, polyamide (Nylon 66), impact modifier, aluminum hydroxide particles, glass fibers, siloxane polymer, and lubricant (Glycolube). The impact modifier was a random copolymer of ethylene and glycidyl methacrylate having 8 wt. % glycidyl methacrylate content and a melt flow index of 5 g/10 min at 190° C. The siloxane polymer was an UHMW functionalized siloxane polymer provided as a masterbatch at 50% siloxane content and 50% resin content. The formulations of each Example are set forth in more detail in the table below.
Once formed, the resulting compositions were then injected molded and tested for various properties as described above. The results are set forth below.
Examples 5-8 were melt mixed using a 32 mm Coperion co-rotating, fully-intermeshing, twin-screw extruder and include various concentrations of a polyarylene sulfide, impact modifier, aluminum hydroxide particles, glass fibers, siloxane polymer, and lubricant (Glycolube). The impact modifier was a random copolymer of ethylene and glycidyl methacrylate having 8 wt. % glycidyl methacrylate content and a melt flow index of 5 g/10 min at 190° C. The siloxane polymer was an UHMW functionalized siloxane polymer provided as a masterbatch at 50% siloxane content and 50% resin content. The formulations of each example are set forth in more detail in the table below.
Once formed, the resulting compositions were then injected molded and tested for various properties as described above. The results are set forth below.
These and other modifications and variations of the present invention may be practiced by those of ordinary skill in the art, without departing from the spirit and scope of the present invention. In addition, it should be understood that aspects of the various embodiments may be interchanged both in whole or in part. Furthermore, those of ordinary skill in the art will appreciate that the foregoing description is by way of example only, and is not intended to limit the invention so further described in such appended claims.
The present application is based upon and claims priority to U.S. Provisional Patent Application Ser. No. 63/422,463, having a filing date of Nov. 4, 2022, which is incorporated herein by reference.
| Number | Date | Country | |
|---|---|---|---|
| 63422463 | Nov 2022 | US |
