The invention relates to ductile and low-warpage, i.e. dimensionally stable, two-component moulded parts which are stress cracking-resistant with respect to the influence of chemicals, in which an amorphous thermoplastic moulding composition as the first component is back-moulded completely or partially with a second likewise amorphous moulding composition as the second component and a stable material bonding of the second to the first component is achieved.
The invention relates moreover to a process for producing the two-component moulded parts by two-component injection moulding and to the use of the two-component moulded parts as, for example, window or glazing modules in construction and in vehicles, ships or aircraft, in lighting applications, as optical lenses with an injection-moulded surround, in car headlight or rear light applications, in non-transparent decorative components back-moulded two-dimensionally with transparent moulding compositions as a high-gloss layer to obtain an effect of depth, as a (backlightable) screen in cars and as a transparent monitor/display cover with a contrasting (for example opaque or translucent and hence backlightable) surround.
Two-component moulded parts in which a transparent or translucent amorphous material has a stable material bonding to a second amorphous material are already known in principle from various areas of application. Polycarbonate, for example, is used as the transparent or translucent amorphous material of the first component. Polycarbonate, or polycarbonate containing glass fibre-filled compositions, and styrene resin are used as materials of the amorphous second component. Such two-component moulded parts known from the prior art have inadequate ductility and/or inadequate stress cracking resistance with respect to the influence of chemicals and/or strong warpage, i.e. deficient dimensional stability, for many areas of application.
The object of this invention was therefore to provide ductile and low-warpage, i.e. dimensionally stable, two-component moulded parts which are stress cracking-resistant with respect to the influence of chemicals, consisting of an amorphous material as the first component and a second amorphous material as the second component.
Surprisingly it was found that the object of the invention is achieved by two-component moulded parts containing
The complete or partial back moulding of the first component (i) with the second component (ii) achieves a bonding of the second component (ii) to the first component (i).
The invention also provides a process for producing the two-component moulded parts by two-component injection moulding, the first component (i) being back-moulded completely or partially with the second component (ii).
In a preferred embodiment
Transparent or translucent amorphous moulding compositions are preferably used as the first component (i).
The preferred constituents a and b of the first component (i) are described below.
Aromatic polycarbonates according to component a which are suitable according to the invention are known from the literature or can be produced by methods known from the literature (regarding the production of aromatic polycarbonates see for example Schnell, “Chemistry and Physics of Polycarbonates”, Interscience Publishers, 1964 and DE-AS 1 495 626, DE-A 2 232 877, DE-A 2 703 376, DE-A 2 714 544, DE-A 3 000 610, DE-A 3 832 396; regarding the production of aromatic polyester carbonates see for example DE-A 3 077 934).
Aromatic polycarbonates are produced for example by reacting diphenols with carbonic acid halides, preferably phosgene, and/or with aromatic dicarboxylic acid dihalides, preferably benzene dicarboxylic acid dihalides, by the interfacial polycondensation process, optionally using chain terminators, for example monophenols, and optionally using trifunctional or higher-functional branching agents, for example triphenols or tetraphenols. Production via a melt polymerisation process by reacting diphenols with diphenyl carbonate, for example, is also possible.
Diphenols for producing the aromatic polycarbonates and/or aromatic polyester carbonates are preferably those of formula (I)
in which
Preferred diphenols are hydroquinone, resorcinol, dihydroxydiphenols, bis(hydroxyphenyl) C1-C5 alkanes, bis(hydroxyphenyl) C5-C6 cycloalkanes, bis(hydroxyphenyl)ethers, bis(hydroxyphenyl) sulfoxides, bis(hydroxyphenyl) ketones, bis(hydroxyphenyl) sulfones and α, α-bis(hydroxyphenyl) diisopropyl benzenes and the ring-brominated and/or ring-chlorinated derivatives thereof.
Particularly preferred diphenols are 4,4′-dihydroxydiphenyl, bisphenol A, 2,4-bis-(4-hydroxyphenyl)-2-methylbutane, 1,1-bis-(4-hydroxyphenyl)cyclohexane, 1,1-bis-(4-hydroxyphenyl)-3.3.5-trimethylcyclohexane, 4,4′-dihydroxydiphenylsulfide, 4,4′-dihydroxydiphenylsulfone and the di- and tetrabrominated or chlorinated derivatives thereof, such as for example 2,2-bis-(3-chloro-4-hydroxyphenyl)propane, 2,2-bis-(3,5-dichloro-4-hydroxyphenyl)propane or 2,2-bis-(3,5-dibromo-4-hydroxyphenyl)propane. 2,2-Bis-(4-hydroxyphenyl)propane (bisphenol A) is preferred in particular.
The diphenols can be used on their own or in any combination. The diphenols are known from the literature or can be obtained by methods known from the literature.
Suitable chain terminators for the production of the thermoplastic, aromatic polycarbonates are for example phenol, p-chlorophenol, p-tert-butylphenol or 2,4,6-tribromophenol, but also long-chain alkylphenols, such as 4-[2-(2,4,4-trimethylpentyl)]phenol, 4-(1,3-tetramethylbutyl)phenol according to DE-A 2 842 005 or monoalkylphenol or dialkylphenols having in total 8 to 20 carbon atoms in the alkyl substituents, such as 3,5-di-tert-butylphenol, p-isooctylphenol, p-tert-octylphenol, p-dodecylphenol and 2-(3,5-dimethylheptyl)phenol and 4-(3,5-dimethylheptyl)phenol. The amount of chain terminators to be used is generally between 0.5 mol % and 10 mol %, relative to the molar sum of the individual diphenols used.
The thermoplastic, aromatic polycarbonates have average weight-average molecular weights (Mw, measured for example by GPC, ultracentrifuge or light-scattering measurement) of 10,000 to 200,000 g/mol, preferably 15,000 to 80,000 g/mol, particularly preferably 24,000 to 32,000 g/mol.
The thermoplastic, aromatic polycarbonates can be branched in a known manner, and preferably by the incorporation of 0.05 to 2.0 mol %, relative to the sum of diphenols used, of trifunctional or higher-functional compounds, for example those having three or more phenolic groups.
Both homopolycarbonates and copolycarbonates are suitable. For the production of copolycarbonates according to component A of the invention, 1 to 25 wt. %, preferably 2.5 to 25 wt. %, relative to the total amount of diphenols to be used, of polydiorganosiloxanes having hydroxyaryloxy end groups can also be used. These are known (U.S. Pat. No. 3,419,634) and can be produced by methods known from the literature. The production of copolycarbonates containing polydiorganosiloxanes is described in DE-A 3 334 782.
Preferred polycarbonates in addition to the bisphenol A homopolycarbonates are the copolycarbonates of bisphenol A having up to 15 mol %, relative to the molar sums of diphenols, of other diphenols cited as being preferred or particularly preferred, in particular 2,2-bis-(3,5-dibromo-4-hydroxyphenyl)propane.
Aromatic dicarboxylic acid dihalides for the production of aromatic polyester carbonates are preferably the diacid dichlorides of isophthalic acid, terephthalic acid, diphenyl ether-4,4′-dicarboxylic acid and naphthalene-2,6-dicarboxylic acid.
Mixtures of the diacid dichlorides of isophthalic acid and terephthalic acid in the ratio between 1:20 and 20:1 are particularly preferred.
A carbonic acid halide, preferably phosgene, is additionally incorporated in the production of polyester carbonates as a bifunctional acid derivative.
In addition to the monophenols already mentioned, the chloroformic acid esters thereof and the acid chlorides of aromatic monocarboxylic acids, which can optionally be substituted by C1 to C22 alkyl groups or by halogen atoms, and aliphatic C2 to C22 monocarboxylic acid chlorides are also suitable as chain terminators for the production of the aromatic polyester carbonates.
The amount of chain terminators in each case is 0.1 to 10 mol %, relative in the case of phenolic chain terminators to mols of diphenol and in the case of monocarboxylic acid chloride chain terminators to mols of dicarboxylic acid dichloride.
The aromatic polyester carbonates can also contain incorporated aromatic hydroxycarboxylic acids.
The aromatic polyester carbonates can be both linear and branched in a known manner (see DE-A 2 940 024 and DE-A 3 007 934 in this respect).
Trifunctional or higher-functional carboxylic acid chlorides, such as trimesic acid trichloride, cyanuric acid trichloride, 3,3′-,4,4′-benzophenone tetracarboxylic acid tetrachloride, 1,4,5,8-naphthalene tetracarboxylic acid tetrachloride or pyromellitic acid tetrachloride, in amounts from 0.01 to 1.0 mol % (relative to dicarboxylic acid dichlorides used), or trifunctional or higher-functional phenols, such as phloroglucinol, 4,6-dimethyl-2,4,6-tri-(4-hydroxyphenyl)hept-2-ene, 4,6-dimethyl-2,4-6-tri-(4-hydroxyphenyl)heptane, 1,3,5-tri-(4-hydroxyphenyl)benzene, 1,1,1-tri-(4-hydroxyphenyl)ethane, tri-(4-hydroxyphenyl)phenylmethane, 2,2-bis[4,4-bis-(4-hydroxy-phenyl)cyclohexyl]propane, 2,4-bis-(4-hydroxyphenyl isopropyl)phenol, tetra-(4-hydroxyphenyl)methane, 2,6-bis-(2-hydroxy-5-methylbenzyl)-4-methyl phenol, 2-(4-hydroxyphenyl)-2-(2,4-dihydroxyphenyl)propane, tetra-(4-[4-hydroxyphenyl isopropyl]phenoxy)methane, 1,4-bis-[4,4′-dihydroxytriphenyl)methyl]benzene, in amounts from 0.01 to 1.0 mol %, relative to diphenols used, can be used for example as branching agents.
Phenolic branching agents can be added with the diphenols, acid chloride branching agents can be introduced together with the acid dichlorides.
The proportion of carbonate structural units in the thermoplastic, aromatic polyester carbonates can vary as required. The proportion of carbonate groups is preferably up to 100 mol %, in particular up to 80 mol %, particularly preferably up to 50 mol %, relative to the sum of ester groups and carbonate groups. Both the ester and the carbonate component of the aromatic polyester carbonates can be present in the form of blocks or be randomly distributed in the polycondensate.
The relative solution viscosity (ηrel) of the aromatic polycarbonates and polyester carbonates is in the range from 1.18 to 1.4, preferably 1.20 to 1.32 (measured in solutions of 0.5 g polycarbonate or polyester carbonate in 100 ml methylene chloride solution at 25° C.).
The thermoplastic, aromatic polycarbonates and polyester carbonates can be used on their own or in any combination.
Polymethyl methacrylate (co)polymers suitable according to the invention as component a are in a preferred embodiment (co)polymers of
These polymethyl methacrylate (co)polymers are resin-like, thermoplastic and rubber-free.
Pure polymethyl methacrylate is particularly preferred.
Production of the polymethyl methacrylate (co)polymers suitable according to the invention as component a takes place by known means by polymerisation of the monomer(s) in bulk, in solution or in dispersion (Kunststoff-Handbuch, vol. IX, Polymethacrylate, Carl Hanser Verlag Munich 1975, pages 22-37).
Polystyrene (co)polymers suitable according to the invention as component a are in a preferred embodiment (co)polymers of
These styrene (co)polymers are resin-like, thermoplastic and rubber-free.
Pure polystyrene is particularly preferred.
Such styrene (co)polymers are known and can be produced by radical polymerisation, in particular by emulsion, suspension, solution or bulk polymerisation. The styrene (co)polymers preferably have average molecular weights Mw (weight-average, determined by GPC, light scattering or sedimentation) of between 15,000 and 250,000.
An aromatic polycarbonate, in particular one based on bisphenol A, is preferably used as component a.
The amorphous first component can contain further additives as component b. Suitable further additives according to component b are in particular conventional polymer additives such as flame retardants (e.g. organic phosphorus or halogen compounds, in particular bisphenol A-based oligophosphate, alkali/alkaline-earth or ammonium/phosphonium salts of perfluorinated sulfonic acids), flame retardant synergists and antidripping agents (for example compounds of the substance classes of fluorinated polyolefins, silicones and aramid fibres), smoke-inhibiting additives (for example boric acid or borates), internal and external lubricants and release agents, for example pentaerythritol tetrastearate or glycidyl monostearate, flowability auxiliaries, antistatics, conductivity additives, stabilisers, for example antioxidants, UV stabilisers, transesterification inhibitors, hydrolysis stabilisers, processing stabilisers, IR absorbers, optical brighteners, fluorescent additives, antibacterial additives, additives to improve scratch resistance, impact modifiers such as for example graft polymers preferably produced by emulsion polymerisation, in a preferred embodiment those having a core-shell structure, fillers and reinforcing materials, preferably in extremely fine-particle, in particular nanoscale form, as well as dyes and pigments.
Amorphous moulding compositions are used as the second component (ii). They are preferably opaque, i.e. non-translucent, materials.
The preferred constituents A, B, C and D of the second component (ii) are described below.
Component A of the second component (ii) corresponds in its embodiments to component a of the first component (i).
Component B is selected from at least one representative from the group of graft polymers B.1 or rubber-free (co)polymers B.2.
Component B.1 comprises one or more graft polymers of
The graft base B.1.2 generally has an average particle size (d50 value) of 0.05 to 10 μm, preferably 0.1 to 5 μm, particularly preferably 0.15 to 2.0 μm.
Monomers B.1.1 are preferably mixtures of
Preferred monomers B.1.1.1 are selected from at least one of the monomers styrene, α-methylstyrene and methyl methacrylate, preferred monomers B.1.1.2 are selected from at least one of the monomers acrylonitrile, maleic anhydride and methyl methacrylate. Particularly preferred monomers are B.1.1.1 styrene and B.1.1.2 acrylonitrile.
Suitable graft bases B.1.2 for the graft polymers B.1 are for example diene rubbers, EP(D)M rubbers, in other words those based on ethylene/propylene and optionally diene, acrylate, polyurethane, silicone, chloroprene and ethylene/vinyl acetate rubbers as well as silicone/acrylate composite rubbers.
Preferred graft bases B.1.2 are diene rubbers, based for example on butadiene and isoprene, or mixtures of diene rubbers or copolymers of diene rubbers or mixtures thereof with further copolymerisable monomers (for example according to B.1.1.1 and B.1.1.2), with the proviso that the glass transition temperature of component B.1.2 is <10° C., preferably <0° C., particularly preferably <−20° C. Pure polybutadiene rubber is particularly preferred.
Particularly preferred polymers B.1 are for example ABS polymers (emulsion, bulk and suspension ABS), such as are described for example in DE-OS 2 035 390 (=U.S. Pat. No. 3,644,574) or in DE-OS 2 248 242 (=GB-PS 1 409 275) or in Ullmanns Enzyklopädie der Technischen Chemie, vol. 19 (1980), p. 280 ff.
The graft copolymers B.1 are produced by radical polymerisation, for example by emulsion, suspension, solution or bulk polymerisation, preferably by emulsion or bulk polymerisation, particularly preferably by emulsion polymerisation.
The gel content of graft base B.1.2 is at least 30 wt. % in the case of graft polymers produced by emulsion polymerisation, preferably at least 40 wt. % (measured in toluene).
The gel content of graft polymers B.1 produced by bulk polymerisation is preferably 10 to 50 wt. %, in particular 15 to 40 wt. % (measured in acetone).
Particularly suitable graft rubbers are also ABS polymers produced by means of redox initiation with an initiator system consisting of organic hydroperoxide and ascorbic acid as described in U.S. Pat. No. 4,937,285.
Since it is known that the graft monomers are not necessarily completely grafted onto the graft base during the graft reaction, according to the invention graft polymers B.1 are also understood to include such products which are obtained by (co)polymerisation of the graft monomers in the presence of the graft base and which co-accumulate during preparation. These products can therefore also contain free, i.e. not chemically bonded to the rubber, (co)polymer of the graft monomers.
In the case of graft polymers B.1 produced by bulk polymerisation the weight-average molecular weight Mw of the free, i.e. not bonded to the rubber, (co)polymer is preferably 50,000 to 250,000 g/mol, in particular 60,000 to 180,000 g/mol, particularly preferably 70,000 to 130,000 g/mol.
Suitable acrylate rubbers according to B.1.2 are preferably polymers of acrylic acid alkyl esters, optionally with up to 40 wt. %, relative to B.1.2, of other polymerisable, ethylenically unsaturated monomers. The preferred polymerisable acrylic acid esters include C1-C8 alkyl esters, for example methyl, ethyl, butyl, n-octyl and 2-ethylhexyl ester; haloalkyl esters, preferably halo C1-C8 alkyl esters, such as chloroethyl acrylate, and mixtures of these monomers.
Monomers having more than one polymerisable double bond can be copolymerised for crosslinking. Preferred examples of crosslinking monomers are esters of unsaturated monocarboxylic acids having 3 to 8 C atoms and unsaturated monohydric alcohols having 3 to 12 C atoms, or saturated polyols having 2 to 4 OH groups and 2 to 20 C atoms, such as ethylene glycol dimethacrylate, allyl methacrylate; polyunsaturated heterocyclic compounds, such as trivinyl and triallyl cyanurate; polyfunctional vinyl compounds, such as divinyl and trivinyl benzenes; but also triallyl phosphate and diallyl phthalate. Preferred crosslinking monomers are allyl methacrylate, ethylene glycol dimethacrylate, diallyl phthalate and heterocyclic compounds having at least three ethylenically unsaturated groups. Particularly preferred crosslinking monomers are the cyclic monomers triallyl cyanurate, triallyl isocyanurate, triacryloyl hexahydro-s-triazine, triallyl benzenes. The amount of crosslinked monomers is preferably 0.02 to 5, in particular 0.05 to 2 wt. %, relative to the graft base B.1.2. In the case of cyclic crosslinking monomers having at least three ethylenically unsaturated groups it is advantageous to restrict the amount to less than 1 wt. % of the graft base B.1.2.
Preferred “other” polymerisable, ethylenically unsaturated monomers which can optionally serve to produce the graft base B.1.2 in addition to the acrylic acid esters are for example acrylonitrile, styrene, α-methylstyrene, acrylamides, vinyl C1-C6 alkyl ethers, methyl methacrylate, butadiene. Preferred acrylate rubbers as the graft base B.2 are emulsion polymers having a gel content of at least 60 wt. %.
Other suitable graft bases according to B.1.2 are silicone rubbers having graft-active sites, such as are described in DE-OS 3 704 657, DE-OS 3 704 655, DE-OS 3 631 540 and DE-OS 3 631 539.
The gel content of graft base B.1.2 or of graft polymers B.1 is determined at 25° C. in a suitable solvent as the insoluble component in these solvents (M. Hoffmann, H. Krömer, R. Kuhn, Polymeranalytik I and II, Georg Thieme-Verlag, Stuttgart 1977).
The average particle size d50 is the diameter above and below which respectively 50 wt. % of the particles lie. It can be determined by ultracentrifuge measurement (W. Scholtan, H. Lange, Kolloid, Z. and Z. Polymere 250 (1972), 782-1796).
Rubber-free vinyl (co)polymers B.2 are rubber-free homo- and/or copolymers of at least one monomer from the group of vinyl aromatics, vinyl cyanides (unsaturated nitriles), (meth)acrylic acid (C1 to C8) alkyl esters, unsaturated carboxylic acids and derivatives (such as anhydrides and imides) of unsaturated carboxylic acids.
Particularly suitable are (co)polymers B.2 consisting of
These (co)polymers B.2 are resin-like, thermoplastic and rubber-free. The copolymer of styrene and acrylonitrile is particularly preferred.
Such (co)polymers B.2 are known and can be produced by radical polymerisation, in particular by emulsion, suspension, solution or bulk polymerisation. The (co)polymers preferably have average molecular weights Mw (weight-average, determined by GPC, light scattering or sedimentation) of between 15,000 and 250,000.
A pure graft polymer B.1 or a mixture of several graft polymers according to B.1, a pure (co)polymer B.2 or a mixture of several (co)polymers according to B.2 or a mixture of at least one graft polymer B.1 and at least one (co)polymer B.2 can be used as component B. If mixtures of several graft polymers, mixtures of several (co)polymers or mixtures of at least one graft polymer and at least one (co)polymer are used, they can be used separately or in the form of a precompound in the production of the compositions according to the invention.
In a preferred embodiment a pure graft polymer B.1 or a mixture of several graft polymers according to B.1 or a mixture of at least one graft polymer B.1 and at least one (co)polymer B.2 is used as component B.
In a particularly preferred embodiment an ABS graft polymer produced by emulsion polymerisation or an ABS graft polymer produced by bulk polymerisation or a mixture of a graft polymer produced by emulsion polymerisation and an SAN copolymer is used as component B.
A naturally occurring or synthetically produced, inorganic isotropic filler is used as component C.
Within the meaning of the invention an isotropic filler is understood to be a filler having a largely isotropic (e.g. spherical or cubic, i.e. dice-shaped) particle geometry. The various dimensions of such particles differ from one another only slightly if at all. The quotient of the largest and the smallest particle dimension in such “isotropic fillers” is no greater than 5, preferably no greater than 3, particularly preferably no greater than 2, in particular no greater than 1.5.
Suitable according to the invention as component C are for example (hollow) glass beads, (hollow) ceramic beads, ground glass fibres, kaolin, carbon black, magnesium hydroxide, aluminium hydroxide, aluminium oxide, boehmite, hydrotalcite, amorphous graphite, quartz, aerosil, other metal or transition metal oxides (for example titanium dioxide or iron oxide), sulfates (for example barium or calcium sulfate), borates (for example zinc borate), carbonates (for example chalk or other forms of calcium carbonate or magnesium carbonate), silicates or alumosilicates (for example ground wollastonite) and nitrides (for example boron nitride).
In particular, the use of the filler in the form of finely-ground types having an average particle diameter d50 of <10 μm, preferably <5 μm, particularly preferably <2 μm, most particularly preferably ≦1.5 μm, is advantageous.
In a preferred embodiment the filler is used in nanoscale form with an average particle diameter d50 of <500 nm, preferably <200 nm, particularly preferably <100 nm, most particularly preferably 5 nm to 80 nm.
The filler can be surface treated, e.g. silanised, in order to ensure a better compatibility with the polymer.
With regard to the processing and production of moulding compositions the use of compacted fillers having an elevated bulk density is advantageous.
The composition can contain further additives as component D. Suitable further additives according to component D include commercial polymer additives selected from the group consisting of flame retardants (for example phosphorus or halogen compounds), flame retardant synergists (for example nanoscale metal oxides), smoke-inhibiting additives (for example boric acid), antidripping agents (for example compounds of the substance classes of fluorinated polyolefins, silicones and aramid fibres), internal and external lubricants and release agents (for example pentaerythritol tetrastearate, montan wax or polyethylene wax), flowability auxiliaries (for example low-molecular-weight vinyl (co)polymers), antistatics (for example block copolymers of ethylene oxide and propylene oxide, other polyethers or polyhydroxy ethers, polyether amides, polyester amides or sulfonic acid salts), conductivity additives (for example conductive carbon black or carbon nanotubes), stabilisers (for example UV/light stabilisers, heat stabilisers, antioxidants, transesterification inhibitors, hydrolysis stabilisers), antibacterial additives (for example silver or silver salts), additives to improve scratch resistance (for example silicone oils), IR absorbers, optical brighteners, fluorescent additives, impact modifiers (for example graft polymers with a rubber core, preferably produced by emulsion polymerisation, which in a particularly preferred embodiment have a core-shell structure), Brønsted acids, platelet-like, scale-like or fibrous fillers and reinforcing materials (for example fibrous wollastonites, glass or carbon fibres, mica, montmorrilonites, layered clay minerals, phyllosilicates, platelet-like kaolin, talc and glass flakes) as well as dyes and pigments differing from component C.
If talc is used as component D, it is used in a concentration of less than 3 wt. %, preferably 0 to 2.5 wt. %, relative to the total composition.
In a preferred embodiment the composition of the second component (ii) is free from talc. In a particularly preferred embodiment the second component (ii) is free from platelet-like, scale-like or fibrous fillers and reinforcing materials.
Phosphorus-containing compounds are preferably used as the flame retardants according to component D. These are preferably selected from the groups of monomeric and oligomeric phosphoric and phosphonic acid esters, phosphonate amines and phosphazenes, wherein mixtures of several components selected from one or more of these groups can also be used as flame retardants. Other halogen-free phosphorus compounds not specifically mentioned here can also be used alone or in any combination with other halogen-free phosphorus compounds.
Preferred monomeric and oligomeric phosphoric or phosphonic acid esters are phosphorus compounds of the general formula (IV)
in which
R1, R2, R3 and R4 preferably independently of one another denote C1 to C4 alkyl, phenyl, naphthyl or phenyl C1-C4 alkyl. The aromatic groups R1, R2, R3 and R4 can in turn be substituted with halogen and/or alkyl groups, preferably chlorine, bromine and/or C1 to C4 alkyl. Particularly preferred aryl radicals are cresyl, phenyl, xylenyl, propyl phenyl or butyl phenyl and the corresponding brominated and chlorinated derivatives thereof.
Mixtures of various phosphates can also be used as component D according to the invention.
Phosphorus compounds of formula (IV) are in particular tributyl phosphate, triphenyl phosphate, tricresyl phosphate, diphenyl cresyl phosphate, diphenyl octyl phosphate, diphenyl-2-ethyl cresyl phosphate, tri(isopropylphenyl) phosphate, resorcinol-bridged oligophosphate and bisphenol A-bridged oligophosphate. The use of oligomeric phosphoric acid esters of formula (IV) derived from bisphenol A is preferred in particular.
Bisphenol A-based oligophosphate according to formula (IVa) is most preferred as component D.
The phosphorus compounds according to component D are known (cf. for example EP-A 0 363 608, EP-A 0 640 655) or can be produced by known methods in an analogous manner (e.g. Ullmanns Enzyklopädie der technischen Chemie, vol. 18, p. 301 ff. 1979; Houben-Weyl, Methoden der organischen Chemie, vol. 12/1, p. 43; Beilstein vol. 6, p. 177).
If mixtures of various phosphorus compounds are used, the specified q value in the case of oligomeric phosphorus compounds is the average q value. The average q value can be determined by determining the composition of the phosphorus compound (molecular weight distribution) by means of suitable methods (gas chromatography (GC), high-pressure liquid chromatography (HPLC), gel permeation chromatography (GPC)) and using this to calculate the average values for q.
Phosphonate amines and phosphazenes as described in WO 00/00541 and WO 01/18105 can also be used as flame retardants.
The flame retardants can be used alone or in any combination with one another or mixed with other flame retardants.
In a preferred embodiment the flame retardants are used in combination with polytetrafluoroethylene (PTFE) as antidripping agent.
The composition of the first component (i) and the second component (ii) is in each case free from crystalline or partially crystalline polymeric constituents; the compositions according to the invention of component (i) and (ii) are in particular free from aromatic or partially aromatic polyesters as disclosed in WO-A 99/28386. Within the meaning of the invention aromatic or partially aromatic polyesters are understood not to be the amorphous polycarbonates which can be used as component a or component A. The aromatic polyesters derive from aromatic dihydroxy compounds and aromatic dicarboxylic acids or aromatic hydroxycarboxylic acids. The partially aromatic polyesters are those based on aromatic dicarboxylic acids and one or more different aliphatic dihydroxy compounds.
Brønsted acids suitable as component D are in principle all types of Brønsted acid organic or inorganic compounds or mixtures thereof.
Preferred organic acids according to component D are selected from at least one of the group of aliphatic or aromatic, optionally polyfunctional, carboxylic acids, sulfonic acids and phosphonic acids. Aliphatic or aromatic dicarboxylic acids and hydroxy-functionalised dicarboxylic acids are preferred in particular.
In a preferred embodiment at least one compound selected from the group consisting of benzoic acid, citric acid, oxalic acid, fumaric acid, mandelic acid, tartaric acid, terephthalic acid, isophthalic acid and p-toluenesulfonic acid is used as component D.
Preferred inorganic acids are ortho- and meta-phosphoric acids and acid salts of these acids as well as boric acid.
The thermoplastic moulding compositions used as the first and second component can be produced for example by mixing the individual constituents in a known manner and melt-compounding and melt-extruding them at temperatures of 200° C. to 360° C., preferably at 240 to 340° C., particularly preferably at 240 to 320° C., in conventional units such as internal mixers, extruders and twin-shaft screws.
Mixing of the individual constituents can take place in a known manner either successively or simultaneously and both at around 20° C. (room temperature) and at elevated temperature.
Production of the low-warpage, i.e. dimensionally stable, ductile two-component parts which are stress cracking-resistant with respect to the influence of chemicals takes place by two-component injection moulding. In this process, after a certain cooling-down time, the transparent or translucent first component is back-moulded completely or partially with the second component, resulting in a stable material bonding of the second to the first component.
These two-component parts can for example be a two-dimensional composite consisting of a transparent or translucent layer with an opaque impact-modified layer, or a composite consisting of a transparent or translucent area framed by an opaque surround. Such composites can be used for example in the windows and glazing sector, in lighting applications, in optical lenses with an opaque injection-moulded surround, in headlight cover discs with an opaque surround, in non-transparent decorative covers back-moulded two-dimensionally with a transparent thermoplastic as a high-gloss layer to obtain an effect of depth, in (backlit) screens in cars and in monitor/display covers with an opaque surround.
Aforementioned two-component parts are preferably produced in a process in which the first component is back-moulded with the second component by injection moulding or injection-compression moulding (two-component injection moulding or two-component injection-compression moulding).
The invention therefore also provides a process for producing the two-component parts according to the invention.
Number | Date | Country | Kind |
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10 2008 048 201.3 | Sep 2008 | DE | national |
Filing Document | Filing Date | Country | Kind | 371c Date |
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PCT/EP2009/006723 | 9/17/2009 | WO | 00 | 4/12/2011 |