EP1910467A1 - Flowable thermoplastic material containing halogen flameproffing agents - Google Patents

Abstract

The invention relates to thermoplastic moulding materials containing A) 10 to 99 % by weight at least one type of thermoplastic polymer, B) 0 to 50 % by weight B1) at least one type of highly- or hyperbranched polycarbonate whose OH index ranges from 1 to 600 mg KOH/g of polycarbonate (according to DIN 53240, Part 2), or (B2) at least one type of highly- or hyperbranched polyester of AxBy type, wherein x is equal to or greater than 1.1 and Y is equal to or greater than 2.1, or the mixture thereof, C) 1 to 30 % by weight flame retardant consisting, in relation to 100 % by weight, C1) 20 to 99 % by weight halogen-containing epoxy resin and C2) 1 to 80 % by weight antiminixide, and D) 0 to 60 % by weight other additives, wherein the sum of percentages by weight of the components from A) to D) is equal to 100 %.

Description

Flowable thermoplastics with halogen flame protection

description

Thermoplastic molding compositions containing

A) 10 to 99% by weight of at least one thermoplastic polymer,

B) 0 to 50% by weight

B1) at least one highly branched or hyperbranched polycarbonate having an OH number of 1 to 600 mg KOH / g polycarbonate (according to DIN 53240, Part 2), or B2) at least one highly branched or hyperbranched polyester of the type A _x B _y with x at least 1, 1 and y at least 2.1 or mixtures thereof

C) 1 to 30 wt .-% of a flame retardant combination, based on 100 wt .-% C),

C1) from 20 to 99% by weight of a halogen-containing epoxy resin, C2) from 1 to 80% by weight of an antimony oxide,

D) 0 to 60 wt .-% of other additives, wherein the sum of the weight percent of components A) to D) gives 100%.

Furthermore, the invention relates to the use of the molding compositions according to the invention for the production of fibers, films and moldings as well as the moldings obtainable in this case of all kinds.

From EP-A 410 301 and EP-A 736 571, for example, halogen-containing flame-retardant polyamides and polyesters are known, in which antimony oxides are mostly used as synergist.

To improve the flowability low molecular weight additives are usually added to thermoplastics. However, the effect of such additives is severely limited because e.g. the decrease in mechanical properties is no longer tolerable when the addition amount of the additive is increased, and the effectiveness of the flame retardant usually also decreases.

From WO-97/45474 thermoplastic compositions are known which contain dendrimeric polyester as AB ₂ molecule in a polyester. Here, a polyhydric alcohol reacts as the core molecule with dimethylpropionic acid as AB2 molecule to a dendrimeric polyester. This contains only OH functionalities at the end of the chain. A disadvantage of these mixtures is the high glass transition temperature of the dendrimeric polyesters, the comparatively complex preparation and above all the poor solubility of the dendrimers in the polyester matrix. According to the teaching of DE-A 101 32 928, the incorporation of such branching agents by means of packaging and postcondensation in the solid phase leads to an improvement in the mechanics (molecular weight build-up). A disadvantage of the method variant described is the long production time and disadvantageous properties already mentioned above.

DE 102004 005652.8 and DE 102004 005657.9 have already proposed new flow-improving additives for polyesters.

It is an object of the present invention to provide thermoplastic, flame-retardant polymer molding compositions which have good flowability and at the same time good mechanical properties and flameproofing properties. In particular, the additive should not bloom or tend to form coating.

Basically, the advantageous effect in the molding compositions according to the invention in thermoplastics of any kind. An enumeration of suitable thermoplastics can be found for example in the plastic paperback (Hrsg. Saechtling), edition 1989, where sources are also called. Processes for the production of such thermoplastics are known per se to the person skilled in the art.

Preferred thermoplastics are selected from the group of polyamides, vinylaromatic polymers, ASA, ABS, SAN polymers, POM, PPE, polyarylene ether sulfones, with polyesters and polycarbonates being preferred.

As component (A), the molding compositions according to the invention contain 10 to 99, preferably 30 to 98.99 and in particular 30 to 95 wt .-% of at least one thermoplastic polymer, preferably polyester / polycarbonates.

Generally, polyesters A) based on aromatic dicarboxylic acids and an aliphatic or aromatic dihydroxy compound are used.

A first group of preferred polyesters are polyalkylene terephthalates, in particular those having 2 to 10 carbon atoms in the alcohol part.

Such polyalkylene terephthalates are known per se and described in the literature. They contain an aromatic ring in the main chain derived from the aromatic dicarboxylic acid. The aromatic ring may also be substituted, for example by halogen, such as chlorine and bromine, or by C 1 -C ₄ -alkyl groups, such as methyl, ethyl, i- or n-propyl and n, i and t-butyl groups. These polyalkylene terephthalates can be prepared by reacting aromatic dicarboxylic acids, their esters or other ester-forming derivatives with aliphatic dihydroxy compounds in a manner known per se.

Preferred dicarboxylic acids are 2,6-naphthalenedicarboxylic acid, terephthalic acid and isophthalic acid or mixtures thereof. Up to 30 mol%, preferably not more than 10 mol% of the aromatic dicarboxylic acids can be replaced by aliphatic or cycloaliphatic dicarboxylic acids such as adipic acid, azelaic acid, sebacic acid, dodecanedioic acids and cyclohexanedicarboxylic acids.

Of the aliphatic dihydroxy compounds are diols having 2 to 6 carbon atoms, in particular 1, 2-ethanediol, 1, 3-propanediol, 1, 4-butanediol, 1,6-hexanediol, 1, 4-hexanediol, 1, 4-cyclohexanediol, 1 , 4-cyclohexanedimethanol and neopentyl glycol or mixtures thereof.

Particularly preferred polyesters (A) are polyalkylene terephthalates which are derived from alkanediols having 2 to 6 C atoms. Of these, particularly preferred are polyethylene terephthalate, polypropylene terephthalate and polybutylene terephthalate or mixtures thereof. Preference is furthermore given to PET and / or PBT which contain up to 1% by weight, preferably up to 0.75% by weight, of 1,6-hexanediol and / or 2-methyl-1,5-pentanediol as further monomer units.

The viscosity number of the polyesters (A) is generally in the range from 50 to 220, preferably from 80 to 160 (measured in a 0.5% strength by weight solution in a phenol / o-dichlorobenzene mixture (wt. 1 at 25 ^° C.) according to ISO 1628.

Particular preference is given to polyesters whose carboxyl end group content is up to 100 meq / kg, preferably up to 50 meq / kg and in particular up to 40 meq / kg of polyester. Such polyesters can be prepared, for example, by the process of DE-A 44 01 055. The carboxyl end group content is usually determined by titration methods (e.g., potentiometry).

Particularly preferred molding compositions contain as component A) a mixture of polyesters which are different from PBT, such as, for example, polyethylene terephthalate (PET). The proportion e.g. of the polyethylene terephthalate is preferably in the mixture up to 50, in particular 10 to 35 wt .-%, based on 100 wt .-% A).

Furthermore, it is advantageous to use PET recyclates (also termed scrap PET), optionally mixed with polyalkylene terephthalates such as PBT.

Recyclates are generally understood as: 1) so-called post-industrial recyclate: this is production waste during polycondensation or during processing, for example, sprues in injection molding, starting goods in injection molding or extrusion or edge sections of extruded sheets or foils.

2) Post Consumer Recyclate: These are plastic items that are collected and processed after use by the end user. By far the dominating items in terms of volume are blow-molded PET bottles for mineral water, soft drinks and juices.

Both types of recycled material can be present either as regrind or in the form of granules. In the latter case, the slag cyclates after separation and purification are melted in an extruder and granulated. This usually facilitates the handling, the flowability and the metering for further processing steps.

Both granulated and regrind recyclates can be used, with the maximum edge length being 10 mm, preferably less than e mm.

Due to the hydrolytic cleavage of polyesters during processing (due to traces of moisture) it is advisable to pre-dry the recyclate. The residual moisture content after drying is preferably <0.2%, in particular <0.05%.

Another group to be mentioned are fully aromatic polyesters derived from aromatic dicarboxylic acids and aromatic dihydroxy compounds.

Suitable aromatic dicarboxylic acids are the compounds already described for the polyalkylene terephthalates. Preference is given to mixtures of 5 to

100 mol% isophthalic acid and 0 to 95 mol% terephthalic acid, in particular mixtures of about 80% terephthalic acid with 20% isophthalic acid to about equivalent mixtures of these two acids used.

The aromatic dihydroxy compounds preferably have the general formula

in the Z, an alkylene or cycloalkylene group having up to 8 C atoms, an arylene group having up to 12 C atoms, a carbonyl group, a sulfonyl group, a Represents oxygen or sulfur atom or a chemical bond and in which m has the value 0 to 2. The compounds may also carry C ₁ -C ₆ -alkyl or alkoxy groups and fluorine, chlorine or bromine as substituents on the phenylene groups.

As a parent of these compounds his example

dihydroxydiphenyl,

Di (hydroxyphenyl) alkane,

Di (hydroxyphenyl) cycloalkane, di (hydroxyphenyl) sulfide,

Di (hydroxyphenyl) ether,

Di (hydroxyphenyl) ketone, di (hydroxyphenyl) sulfoxide, α, α'-di- (hydroxyphenyl) dialkylbenzene, di (hydroxyphenyl) sulfone, di (hydroxybenzoyl) benzene

Resorcinol and

Hydroquinone and their kemalkylierte or kemhalogenierte derivatives called.

Of these will be

4,4'-dihydroxydiphenyl,

2,4-di- (4'-hydroxyphenyl) -2-methylbutane σ, σ'-di- (4-hydroxyphenyl) -p-diisopropylbenzene,

2,2-di- (3'-methyl-4'-hydroxyphenyl) propane and 2,2-di (3'-chloro-4'-hydroxyphenyl) propane,

and in particular

2,2-di (4'-hydroxyphenyl) propane 2,2-di (3 ', 5-dichlorodihydroxyphenyl) propane,

1, 1-di- (4'-hydroxyphenyl) cyclohexane,

3,4'-dihydroxybenzophenone,

4,4'-dihydroxydiphenylsulfone and

2,2-di (3 ', 5'-dimethyl-4'-hydroxyphenyl) propane

or mixtures thereof are preferred.

Of course, it is also possible to use mixtures of polyalkylene terephthalates and wholly aromatic polyesters. These generally contain from 20 to 98% by weight of the polyalkylene terephthalate and from 2 to 80% by weight of the wholly aromatic polyester. Of course, polyester block copolymers such as copolyetheresters may also be used. Such products are known per se and described in the literature, for example in US Pat. No. 3,651,014. Also in the trade corresponding products are available, eg Hytrel® (DuPont).

As a polyester to be understood according to the invention also halogen-free polycarbonates. Suitable halogen-free polycarbonates are, for example, those based on diphenols of the general formula

wherein Q is a single bond, a C ₁ to C ₈ alkylene, a C ₂ to C ₃ alkylidene, a C ₃ to C ₆ cycloalkylidene group, a C ₆ to C ₁₂ arylene group, and -O- , -S- or -SO ₂ - and m is an integer from 0 to 2.

The diphenols may also have substituents on the phenylene radicals, such as C ₁ - to Ce-alkyl or C ₁ - to C ₆ -alkoxy.

Preferred diphenols of the formula are, for example, hydroquinone, resorcinol, 4,4'-dihydroxydiphenyl, 2,2-bis (4-hydroxyphenyl) propane, 2,4-bis (4-hydroxyphenyl) -2-methylbutane, 1, 1 bis (4-hydroxyphenyl) -cyclohexane. Particularly preferred are 2,2-bis (4-hydroxyphenyl) propane and 1, 1-bis (4-hydroxyphenyl) cyclohexane, and 1, 1-bis (4-hydroxyphenyl) -3,3,5- trimethylcyclohexane.

Both homopolycarbonates and copolycarbonates are suitable as component A, and in addition to the bisphenol A homopolymer, the copolycarbonates of bisphenol A are preferred.

The suitable polycarbonates may be branched in a known manner, preferably by the incorporation of from 0.05 to 2.0 mol%, based on the sum of the diphenols used, of at least trifunctional compounds, for example those having three or more than three phenolic compounds OH groups.

Particularly suitable polycarbonates have proven, the relative viscosities / 7 _re i from 1, 10 to 1, 50, in particular from 1, 25 to 1, 40 have. This corresponds to average molecular weights M _w (weight average) of from 10,000 to 200,000, preferably from 20,000 to 80,000 g / mol.

The diphenols of the general formula are known per se or can be prepared by known processes. The polycarbonates can be prepared, for example, by reacting the diphenones with phosgene by the phase boundary process or with phosgene by the homogeneous phase process (the so-called pyridine process), the molecular weight to be set in each case being achieved in a known manner by a corresponding amount of known chain terminators , (With regard to polydiorganosiloxane-containing polycarbonates, see for example DE-OS 33 34 782).

Suitable chain terminators are, for example, phenol, p-t-butylphenol but also long-chain alkylphenols such as 4- (1, 3-tetramethyl-butyl) -phenol, according to

DE-OS 28 42 005 or monoalkylphenols or dialkylphenols having a total of 8 to 20 C atoms in the alkyl substituents according to DE-A 35 06 472, such as p-nonylphenyl, 3,5-di-t-butylphenol, pt-octylphenol, p- Dodecylphenol, 2- (3,5-dimethyl-heptyl) -phenol and 4- (3,5-dimethylheptyl) -phenol.

Halogen-free polycarbonates in the context of the present invention means that the polycarbonates are composed of halogen-free diphenols, halogen-free chain terminators and optionally halogen-free branching agents, the content of minor ppm amounts of saponifiable chlorine, resulting, for example, from the preparation of the polycarbonates with phosgene by the interfacial process, is not to be regarded as halogen-containing in the context of the invention. Such polycarbonates with ppm contents of saponifiable chlorine are halogen-free polycarbonates in the context of the present invention.

As further suitable components A) may be mentioned amorphous polyester carbonates, wherein phosgene was replaced by aromatic dicarboxylic acid units such as isophthalic acid and / or terephthalic acid units in the preparation. For further details, reference is made to EP-A 711 810 at this point.

Further suitable copolycarbonates with cycloalkyl radicals as monomer units are described in EP-A 365 916.

Furthermore, bisphenol A can be replaced by bisphenol TMC. Such polycarbonates are available under the trademark APEC HT® from Bayer.

As component B), the molding compositions of the invention 0 to 50, preferably 0.01 to 40 and in particular 0.7 to 10 wt .-% B1) of at least one highly branched or hyperbranched polycarbonate having an OH number of 1 to 600, preferably 10 to 550 and in particular from 50 to 550 mg KOH / g polycarbonate (according to DIN 53240, Part 2) or at least one hyperbranched polyester as component B2) or mixtures thereof as described below. Hyperbranched polycarbonates B1) in the context of this invention are understood to mean crosslinked macromolecules having hydroxyl groups and carbonate groups which are structurally as well as molecularly nonuniform. They can be constructed on the one hand, starting from a central molecule analogous to dendrimers, but with uneven chain length of the branches. On the other hand, they can also be constructed linearly with functional side groups or, as a combination of the two extremes, they can have linear and branched molecular parts. For the definition of dendrimeric and hyperbranched polymers see also PJ. Flory, J. Am. Chem. Soc. 1952, 74, 2718 and H. Frey et al., Chem. Eur. J. 2000, 6, no. 14, 2499.

By "hyperbranched" in the context of the present invention is meant that the degree of branching (DB), ie the average number of dendritic linkages plus average number of end groups per molecule, is 10 to 99.9%, preferably 20 to 99%, particularly preferably 20-95%.

By "dendrimer" in the context of the present invention is meant that the degree of branching is 99.9-100% For definition of the "degree of branching" see H. Frey et al., Acta Polym. 1997, 48, 30.

Preferably, component B1) has a number average molecular weight M _{n of} from 100 to 15,000, preferably from 200 to 12,000 and in particular from 500 to 10,000 g / mol (GPC, standard PMMA).

The glass transition temperature Tg is in particular from -8O ⁰ C to +140, preferably from -60 to 12O ⁰ C (according to DSC, DIN 53765).

In particular, the viscosity (mPas) at 23 ° C. (in accordance with DIN 53019) is from 50 to 200,000, in particular from 100 to 150,000, and very particularly preferably from 200 to 100,000.

Component B1) is preferably obtainable by a process comprising at least the following steps:

a) reacting at least one organic carbonate (A) of the general formula RO [(CO)] _n OR with at least one aliphatic, aliphatic / aromatic or aromatic alcohol (B) which has at least 3 OH groups, with elimination of alcohols ROH to one or more condensation products (K), wherein Rjeweils independently each other is a straight-chain or branched aliphatic, aromatic / aliphatic or aromatic see hydrocarbon radical having 1 to 20 carbon atoms, and wherein the radicals R also under Forming a ring can be connected to each other and n represents an integer between 1 and 5, or G

ab) reaction of phosgene, diphosgene or triphosgene with o.g. Alcohol (B) with elimination of hydrogen chloride

such as

b) intermolecular conversion of the condensation products (K) into a highly functional, highly branched or hyperbranched polycarbonate,

wherein the quantitative ratio of the OH groups to the carbonates in the reaction mixture is selected so that the condensation products (K) have on average either a carbonate group and more than one OH group or one OH group and more than one carbonate group.

The starting material used may be phosgene, diphosgene or triphosgene, organic carbonates being preferred.

The radicals R used as starting material organic carbonates (A) of the general formula RO (CO) _n OR are each independently a straight-chain or branched aliphatic, aromatic / aliphatic or aromatic hydrocarbon radical having 1 to 20 carbon atoms. The two radicals R can also be linked together to form a ring. It is preferably an aliphatic hydrocarbon radical and particularly preferably a straight-chain or branched alkyl radical having 1 to 5 C atoms, or a substituted or unsubstituted phenyl radical.

In particular, simple carbonates of the formula RO (CO) _n OR are used; n is preferably 1 to 3, in particular 1.

Dialkyl or diaryl carbonates can be prepared, for example, from the reaction of aliphatic, araliphatic or aromatic alcohols, preferably monoalcohols with phosgene. Furthermore, they can also be prepared via oxidative carbonylation of the alcohols or phenols by means of CO in the presence of noble metals, oxygen or NO _x . For preparation methods of diaryl or dialkyl carbonates, see also "Ulimann ^'s Encyclopedia of Industrial Chemistry", 6th Edition, 2000 Electronic Release, published by Wiley-VCH.

Examples of suitable carbonates include aliphatic, aromatic / aliphatic or aromatic carbonates, such as ethylene carbonate, 1, 2 or 1, 3-propylene carbonate, diphenyl carbonate, ditolyl carbonate, dixylyl carbonate, dinaphthyl carbonate, ethyl phenyl carbonate, dibenzyl carbonate, dimethyl carbonate, diethyl carbonate, dipropyl carbonate, dibutyl carbonate, diisobutyl carbonate, dipentyl carbonate, dihexyl carbonate, dicyclohexyl carbonate, diheptyl carbonate, dioctyl carbonate, didecylacarbonate or didodecyl carbonate.

Examples of carbonates in which n is greater than 1 include dialkyl dicarbonates such as di (-t-butyl) dicarbonate or dialkyl tricarbonates such as di (-t-butyl tricarbonate).

Aliphatic carbonates are preferably used, in particular those in which the radicals comprise 1 to 5 C atoms, for example dimethyl carbonate, diethyl carbonate, dipropyl carbonate, dibutyl carbonate or diisobutyl carbonate.

The organic carbonates are reacted with at least one aliphatic alcohol (B) which has at least 3 OH groups or mixtures of two or more different alcohols.

Examples of compounds having at least three OH groups include glycerol, trimethylolmethane, trimethylolethane, trimethylolpropane, 1, 2,4-butanetriol, tris (hydroxymethyl) amine, tris (hydroxyethyl) amine, tris (hydroxypropyl) amine, pentaerythritol, Diglycerine, triglycerol, polyglycerols, bis (tri-methylolpropane), tris (hydroxymethyl) isocyanurate, tris (hydroxyethyl) isocyanurate, phloroglucinol ,, trihydroxytoluene, trihydroxydimethylbenzene, phloroglucide, hexahydroxybenzene, 1,3,5-benzenetrimethanol, 1, 1,1-tris (4'-hydroxyphenyl) methane, 1,1,1-tris (4'-hydroxyphenyl) ethane or sugars, for example glucose, tri- or higher-functional polyetherols based on tri- or higher-functional alcohols and Ethylene oxide, propylene oxide or butylene oxide, or polyesterols. Glycerol, trimethylolethane, trimethylolpropane, 1, 2,4-butanetriol, pentaerythritol and their polyetherols based on ethylene oxide or propylene oxide are particularly preferred.

These polyhydric alcohols can also be used in mixture with difunctional alcohols (B ^' ), with the proviso that the mean OH functionality of all the alcohols used together is greater than 2. Examples of suitable compounds having two OH groups include ethylene glycol, diethylene glycol, triethylene glycol, 1, 2 and 1, 3-propanediol, dipropylene glycol, tripropylene glycol, neopentyl glycol, 1, 2, 1, 3 and 1, 4-butanediol, 1, 2-, 1, 3- and 1,5-pentanediol, hexanediol, cyclopentanediol, cyclohexanediol, cyclohexanedimethanol, bis (4-hydroxycyclohexyl) methane, bis (4-hydroxycyclohexyl) ethane, 2,2-bis (4- Hydroxycyclohexyl) propane, 1, 1'-bis (4-hydroxyphenyl) -3,3-5-trimethylcyclohexane, resorcinol, hydroquinone, 4,4'-dihydroxyphenyl, bis (4-bis (hydroxyphenyl) sulfide, bis ( 4-hydroxyphenyl) sulfone, bis (hydroxymethyl) benzene, bis (hydroxymethyl) toluene, bis (p-hydroxyphenyl) methane, bis (p-hydroxyphenyl) ethane, 2,2-bis (p-hydroxyphenyl) propane, 1, 1-bis (p-hydroxyphenyl) cyclohexane, dihydroxybenzophenone, difunctional polyether polyols based on ethylene oxide, propylene oxide, butylene oxide or their mixtures, polytetrahydrofuran, polycaprolactone or polyesterols based on diols and dicarboxylic acids.

The diols serve to finely adjust the properties of the polycarbonate. If di-functional alcohols are used, the ratio of difunctional alcohols B ') to the at least trifunctional alcohols (B) is determined by the person skilled in the art according to the desired properties of the polycarbonate. In general, the amount of the alcohol or alcohols (B ') is 0 to 39.9 mol% with respect to the total amount of all alcohols (B) and (B') together. The amount is preferably 0 to 35 mol%, more preferably 0 to 25 mol% and most preferably 0 to 10 mol%.

The reaction of phosgene, diphosgene or triphosgene with the alcohol or alcohol mixture is generally carried out with the elimination of hydrogen chloride, the reaction of the carbonates with the alcohol or alcohol mixture to give the highly functional highly branched polycarbonate according to the invention takes place with elimination of the monofunctional alcohol or phenol from the carbonate. Molecule.

The highly functional highly branched polycarbonates formed by the process according to the invention are terminated after the reaction, ie without further modification, with hydroxyl groups and / or with carbonate groups. They dissolve well in various solvents, for example in water, alcohols, such as methanol, ethanol, butanol, alcohol / water mixtures, acetone, 2-butanone, ethyl acetate, butyl acetate, methoxypropyl acetate, methoxyethyl acetate, tetrahydrofuran, dimethylformamide, dimethylacetamide, N-methylpyrrolidone, ethylene carbonate or propylene carbonate.

In the context of this invention, a high-functionality polycarbonate is to be understood as meaning a product which, in addition to the carbonate groups which form the polymer backbone, also has at least three, preferably at least six, more preferably at least ten functional groups. The functional groups are carbonate groups and / or OH groups. In principle, the number of terminal or pendant functional groups is not limited to the top, but products having a very large number of functional groups may have undesirable properties such as high viscosity or poor solubility. The high-functionality polycarbonates of the present invention generally have not more than 500 terminal or pendant functional groups, preferably not more than 100 terminal or pendant functional groups.

In the preparation of the high-functionality polycarbonates B1), it is necessary to adjust the ratio of compounds containing OH groups to phosgene or carbonates so that the resulting simplest condensation product (referred to hereinafter as condensation product (K)) either a carbonate group or Carbamoyl group and more than one OH group or one OH group and more than contains a carbonate group or carbamoyl group. The simplest structure of the condensation product (K) of a carbonate (A) and a di- or Polyaikohol (B) gives the arrangement XY _n or Y _n X, where X is a carbonate group, Y is a hydroxyl group and n usually one Number between 1 and 6, preferably between 1 and 4, more preferably between 1 and 3. The reactive group, which results as a single group, is referred to hereinafter generally "focal group".

If, for example, in the preparation of the simplest condensation product (K) from a carbonate and a dihydric alcohol, the reaction ratio is 1: 1, the average results in a molecule of the type XY, illustrated by the general formula 1.

Rv _Q 1

In the preparation of the condensation product (K) from a carbonate and a trihydric alcohol at a conversion ratio of 1: 1 results in the average molecule of the type XY2, illustrated by the general formula 2. Focal group here is a carbonate group.

In the preparation of the condensation product (K) from a carbonate and a tetrahydric alcohol also with the conversion ratio 1: 1 results in the average, a molecule of the type XY3, illustrated by the general formula 3. Focal group here is a carbonate group.

In the formulas 1 to 3, R has the meaning defined above and R ¹ is an aliphatic or aromatic radical.

Further, the preparation of the condensation product (K) may be, for example, also made of a carbonate and a trihydric alcohol exemplified by the general one Formula 4, carried out, wherein the reaction ratio is at molar 2: 1. This results in the average molecule of type X2Y, focal group here is an OH group. In the formula 4, R and R ^{1 have} the same meaning as in the formulas 1 to 3.

If, in addition to the components, difunctional compounds, e.g. given a dicarbonate or a diol, this causes an extension of the chains, as illustrated for example in the general formula 5. The result is again on average a molecule of the type XY2, focal group is a carbonate group.

In formula 5, R ^{2 is} an organic, preferably aliphatic radical, R and R ¹ are defined as described above.

It is also possible to use a plurality of condensation products (K) for the synthesis. In this case, on the one hand, several alcohols or more carbonates can be used. Furthermore, mixtures of different condensation products of different structure can be obtained by selecting the ratio of the alcohols used and the carbonates or phosgene. This is exemplified by the example of the reaction of a carbonate with a trihydric alcohol. If the starting materials are used in a ratio of 1: 1, as shown in (II), a molecule of XY _{2 is obtained} . If the starting materials are used in a ratio of 2: 1, as shown in (IV), one molecule X2Y is obtained. At a ratio between 1: 1 and 2: 1, a mixture of molecules XY2 and X2Y is obtained.

The simple condensation products (K) described by way of example in the formulas 1 to 5 preferably react according to the invention intermolecularly to form highly functional polycondensation products, referred to hereinafter as polycondensation products (P). The reaction to give the condensate (K) and the polycondensation product (P) is usually carried out at a temperature of 0 to 250 ^° C ₁ preferably 60 to 160 ° C in bulk or in solution. In general, all solvents can be used which are inert to the respective starting materials. Preference is given to using organic solvents, for example decane, dodecane, benzene, toluene, chlorobenzene, xylene, dimethylformamide, dimethylacetamide or solvent naphtha.

In a preferred embodiment, the condensation reaction is carried out in bulk. The monofunctional alcohol ROH or phenol liberated in the reaction can be removed from the reaction equilibrium by distillation, optionally under reduced pressure, to accelerate the reaction.

If distilling off is intended, it is regularly advisable to use those carbonates which release alcohols ROH having a boiling point of less than 140 ^° C. during the reaction.

To accelerate the reaction, it is also possible to add catalysts or catalyst mixtures. Suitable catalysts are compounds which catalyze esterification or transesterification reactions, for example alkali metal hydroxides, alkali metal carbonates, alkali metal hydrogencarbonates, preferably of sodium, potassium or cesium, tertiary amines, guanidines, ammonium compounds, phosphonium compounds, aluminum, tin, zinc, Titanium, zirconium or bismuth organic compounds, also called double metal cyanide (DMC) catalysts, as described for example in DE 10138216 or in DE 10147712.

Preference is given to potassium hydroxide, potassium carbonate, potassium bicarbonate, diazabicyclooctane (DABCO), diazabicyclononene (DBN), diazabicycloundecene (DBU), imidazoles, such as imidazole, 1-methylimidazole or 1,2-dimethylimidazole, titanium tetrabutylate, titanium tetraisopropylate, dibutyltin oxide, Dibutyltin dilaurate, Zinndioctoat, Zirkonacetyla- cetonate or mixtures thereof used.

The addition of the catalyst is generally carried out in an amount of 50 to 10,000, preferably from 100 to 5000 ppm by weight, based on the amount of the alcohol or alcohol mixture used.

Furthermore, it is also possible to control the intermolecular polycondensation reaction both by adding the appropriate catalyst and by selecting a suitable temperature. Furthermore, the average molecular weight of the polymer (P) can be adjusted via the composition of the starting components and over the residence time.

The condensation products (K) or the polycondensation products (P), which were prepared at elevated temperature, are usually stable at room temperature for a longer period. Due to the nature of the condensation products (K), it is possible that the condensation reaction may result in polycondensation products (P) having different structures which have branches but no crosslinks. In addition, the polycondensation products (P) ideally have either a carbonate group as a focal group and more than two OH groups or else an OH group as a focal group and more than two carbonate groups. The number of reactive groups results from the nature of the condensation products used (K) and the degree of polycondensation.

For example, a condensation product (K) according to the general formula 2 by three-fold intermolecular condensation to two different polycondensation onsprodukten (P), which are represented in the general formulas 6 and 7, react.

In formulas 6 and 7, R and R ^{1 are} as defined above.

There are various possibilities for stopping the intermolecular polycondensation reaction. For example, the temperature can be lowered to a range in which the reaction comes to a standstill and the product (K) or the polycondensation product (P) is storage-stable.

Furthermore, one can deactivate the catalyst, in basic eg by addition of Lewis acids or protic acids. In a further embodiment, as soon as a polycondensation product (P) with the desired degree of polycondensation is present due to the intermolecular reaction of the condensation product (K), the product (P) to terminate the reaction is added to a product having groups which are reactive towards the focal group of (P) - the. For example, in the case of a carbonate group as the focal group, a mono-, di- or poly-amine may be added. In the case of a hydroxyl group as the focal group, the product (P) can be added, for example, to a mono-, di- or polyisocyanate, an epoxy-group-containing compound or an OH derivative reactive acid derivative.

The preparation of the high-functionality polycarbonates according to the invention is usually carried out in a pressure range from 0.1 mbar to 20 bar, preferably at 1 mbar to 5 bar, in reactors or reactor cascades which are operated batchwise, semicontinuously or continuously.

By the aforementioned adjustment of the reaction conditions and optionally by the choice of the suitable solvent, the products according to the invention can be further processed after preparation without further purification.

In a further preferred embodiment, the product is stripped, that is, freed from low molecular weight, volatile compounds. For this, after reaching the desired degree of conversion, the catalyst can optionally be deactivated and the low molecular weight volatiles, e.g. Monoalcohols, phenols, carbonates, hydrogen chloride or volatile olfgomere or cyclic compounds by distillation, optionally with the introduction of a gas, preferably nitrogen, carbon dioxide or air, optionally at reduced pressure, are removed.

In a further preferred embodiment, the polycarbonates according to the invention can be given, in addition to the functional groups already obtained by the reaction, further functional groups. The functionalization can during the molecular weight build-up or even subsequently, i. take place after completion of the actual polycondensation.

If components are added before or during the molecular weight build-up which have other functional groups or functional groups in addition to hydroxyl or carbonate groups, a polycarbonate polymer having randomly distributed functionalities other than the carbonate or hydroxyl groups is obtained.

Such effects can be achieved, for example, by addition of compounds during the polycondensation which, in addition to hydroxyl groups, carbonate groups or carbamoyl groups, contain further functional groups or functional elements, such as mercapto groups, primary, secondary or tertiary amino groups, ether groups, derivatives of carboxylic acids, derivatives of sulfonic acids, derivatives of phosphonic acids, silane groups, siloxane groups, aryl radicals or long-chain alkyl radicals. For modification by means of carbamate groups, for example, ethanolamine, propanolamine, isopropanolamine, 2- (butylamino) ethanol, 2- (cyclohexylamino) ethanol, 2-amino-1-butanol, 2- (2 ^' aminoethoxy) ethanol or higher can be Use alkoxylation products of ammonia, 4-hydroxy-piperidine, 1-hydroxyethylpiperazine, diethanolamine, dipropanolamine, diisopropanolamine, tris (hydroxymethyl) aminomethane, tris (hydroxyethyl) amino methane, ethylene diamine, propylene diamine, hexamethylene diamine or isophorone diamine.

Mercaptoethanol can be used for the modification with mercapto groups, for example. Tertiary amino groups can be produced, for example, by incorporation of N-methyldiethanolamine, N-methyldipropanolamine or N, N-dimethylethanolamine. Ether groups can be generated, for example, by condensation of di- or higher-functional polyetherols. Long-chain alkyl radicals can be introduced by reaction with long-chain alkanediols, the reaction with alkyl or aryl diisocyanates generates polycarbonates containing alkyl, aryl and urethane groups or urea groups.

By adding dicarboxylic acids, tricarboxylic acids, e.g. Terephthalic acid dimethyl esters or tricarboxylic acid esters can be produced ester groups.

Subsequent functionalization can be obtained by reacting the resulting highly functional, highly branched or hyperbranched polycarbonate in an additional process step (step c)) with a suitable functionalizing reagent which reacts with the OH and / or carbonate groups or carbamoyl groups of the polycarbonate can react, converts.

Hydroxyl-containing, highly functional, highly branched or hyperbranched polycarbonates can be modified, for example, by addition of molecules containing acid groups or isocyanate groups. For example, polycarbonates containing acid groups can be obtained by reaction with compounds containing anhydride groups.

Furthermore, hydroxyl-containing high-functionality polycarbonates can also be converted into highly functional polycarbonate-polyether polyols by reaction with alkylene oxides, for example ethylene oxide, propylene oxide or butylene oxide.

A big advantage of the method lies in its economy. Both the conversion to a condensation product (K) or polycondensation product (P) and the reaction of (K) or (P) to polycarbonates with other functional groups or elements may be in a reaction device, which is technically and economically advantageous.

As component B2), the molding compositions according to the invention may contain at least one hyperbranched polyester of the type A _x B _y , where

x at least 1, preferably at least 1, 3, in particular at least 2 y at least 2.1, preferably at least 2.5, in particular at least 3

is.

Of course, mixtures may also be used as units A and B, respectively.

A polyester of the type A _x B _y is understood to mean a condensate which is composed of an x-functional molecule A and a y-functional molecule B. For example, mention may be made of a polyester of adipic acid as molecule A (x = 2) and glycerol as molecule B (y = 3).

Hyperbranched polyesters B2) in the context of this invention are understood to mean undecomposed macromolecules having hydroxyl and carboxyl groups which are structurally as well as molecularly nonuniform. They can be constructed on the one hand, starting from a central molecule analogous to dendrimers, but with uneven chain length of the branches. On the other hand, they can also be constructed linearly with functional side groups or, as a combination of the two extremes, they can have linear and branched molecular parts. For the definition of dendrimeric and hyperbranched polymers see also PJ. Flory, J. Am. Chem. Soc. 1952, 74, 2718 and H. Frey et al., Chem. Eur. J. 2000, 6, no. 14, 2499.

By "hyperbranched" in the context of the present invention is meant that the degree of branching (DB), ie the average number of dendritic linkages plus average number of end groups per molecule, is 10 to 99.9%, preferably 20 to 99%, more preferably 20-95%. "Dendrimer" in the context of the present invention is understood to mean that the degree of branching is 99.9-100%. For the definition of the degree of branching see H. Frey et al., Acta Polym. 1997, 48, 30.

The component B2) preferably has an M _n of 300 to 30,000, in particular from 400 to 25,000 and very particularly from 500 to 20,000 g / mol, determined by means of GPC, standard PMMA, mobile phase dimethylacetamide. Preferably, B2) has an OH number of 0 to 600, preferably 1 to 500, in particular from 20 to 500 mg KOH / g polyester according to DIN 53240 and preferably a COOH number of 0 to 600, preferably from 1 to 500 and in particular from 2 to 500 mg KOH / g polyester.

The T ₉ is preferably from -5O ⁰ C to 140 ° C and in particular from -50 to 100 ⁰ C (by DSC, according to DIN 53765).

In particular, such components B2) are preferred in which at least one OH or COOH number is greater than 0, preferably greater than 0.1 and in particular greater than 0.5.

In particular, by the methods described below, the inventive component B2) is available, u.z. by

(A) one or more dicarboxylic acids or one or more derivatives thereof with one or more at least trifunctional alcohols

or

(b) one or more tricarboxylic acids or higher polycarboxylic acids or one or more derivatives thereof with one or more diols

in the presence of a solvent and optionally in the presence of an inorganic, organometallic or low molecular weight organic catalyst or an enzyme. The reaction in the solvent is the preferred method of preparation.

Highly functional hyperbranched polyesters B2) in the context of the present invention are molecularly and structurally nonuniform. They differ in their molecular heterogeneity of dendrimers and are therefore produced with considerably less effort.

The dicarboxylic acids which can be reacted according to variant (a) include, for example, oxalic acid, malonic acid, succinic acid, glutaric acid, adipic acid, pimelic acid, suberic acid, sebacic acid, undecane-α, ω-dicarboxylic acid, dodecane-α, ω-dicarboxylic acid, cis- and trans- Cyclohexane-1,2-dicarboxylic acid, cis- and trans-

Cyclohexane-1,3-dicarboxylic acid, cis- and trans -cyclohexane-1,4-dicarboxylic acid, cis- and trans-cyclopentane-1,2-dicarboxylic acid and also cis- and trans-cyclopentane-1,3-dicarboxylic acid,

wherein the above-mentioned dicarboxylic acids may be substituted with one or more radicals selected from C 1 -C 10 -alkyl groups, for example methyl, ethyl, n-propyl, isopropyl, n-butyl, isobutyl, sec-butyl, tert-butyl, n-pentyl, isopentyl, sec-pentyl, neo-pentyl, 1, 2-dimethylpropyl, iso-amyl, n-hexyl, iso -hexyl, sec-hexyl, n-heptyl, iso-heptyl, n-octyl, 2-ethylhexyl, n-nonyl or n-decyl .

C 3 -C 12 -cycloalkyl groups, for example cyclopropyl, cyclobutyl, cyclopentyl, cyclohexyl, cycloheptyl, cyclooctyl, cyclononyl, cyclodecyl, cycloundecyl and cyclododecyl; preferred are cyclopentyl, cyclohexyl and cycloheptyl;

Alkylene groups such as methylene or ethylidene or

C6-Ci ₄ aryl groups such as phenyl, 1-naphthyl, 2-naphthyl, 1-anthryl, 2- anthryl, 9-anthryl, 1-phenanthryl, 2-phenanthryl, 3-phenanthryl, 4-phenanthryl and 9-phenanthryl, preferably phenyl, 1-naphthyl and 2-naphthyl, particularly preferably phenyi.

Examples of substituted dicarboxylic acids include: 2-methylmalonic acid, 2-ethylmalonic acid, 2-phenylmalonic acid, 2-methylsuccinic acid, 2-ethylsuccinic acid, 2-phenylsuccinic acid, itaconic acid, 3,3-dimethylglutaric acid.

Furthermore, the dicarboxylic acids which can be reacted according to variant (a) include ethylenically unsaturated acids, such as, for example, maleic acid and fumaric acid, and aromatic dicarboxylic acids, for example phthalic acid, isophthalic acid or terephthalic acid.

Furthermore, mixtures of two or more of the aforementioned representatives can be used.

The dicarboxylic acids can be used either as such or in the form of derivatives.

Derivatives are preferably understood

the relevant anhydrides in monomeric or polymeric form,

Mono- or dialkyl esters, preferably mono- or dimethyl esters or the corresponding mono- or diethyl esters, but also those of higher alcohols such as n-propanol, iso-propanol, n-butanol, isobutanol, tert-butanol, n-pentanol, n Hexanol-derived mono- and dialkyl esters,

furthermore mono- and divinyl esters as well mixed esters, preferably methyl ethyl esters.

Within the scope of the preferred preparation, it is also possible to use a mixture of a dicarboxylic acid and one or more of its derivatives. Likewise, it is possible to use a mixture of several different derivatives of one or more dicarboxylic acids.

Succinic acid, glutaric acid, adipic acid, phthalic acid, isophthalic acid, terephthalic acid or their mono- or dimethyl esters are particularly preferably used. Most preferably, adipic acid is used.

As at least trifunctional alcohols, for example, can be implemented: glycerol, butane-1, 2,4-triol, n-pentane-1, 2,5-triol, n-pentane-1, 3,5-triol, n-hexane-1 , 2,6-triol, n-hexane-1, 2,5-triol, n-hexane-1, 3,6-triol, trimethylolbutane, trimethylolpropane or di-trimethylolpropane, trimethylolethane, pentaerythritol or dipentaerythritol; Sugar alcohols such as mesoerythritol, threitol, sorbitol, mannitol or mixtures of the above at least trifunctional alcohols. Glycerol, trimethylolpropane, trimethylolethane and pentaerythritol are preferably used.

According to variant (b) convertible tricarboxylic acids or polycarboxylic acids are, for example, 1, 2,4-benzenetricarboxylic acid, 1, 3,5-benzenetricarboxylic acid, 1, 2,4,5-Benzoltetra- carboxylic acid and mellitic acid.

Tricarboxylic acids or polycarboxylic acids can be used in the reaction according to the invention either as such or in the form of derivatives.

Derivatives are preferably understood

the relevant anhydrides in monomeric or polymeric form,

Mono-, di- or trialkyl, preferably mono-, di- or trimethyl esters or the corresponding mono-, di- or triethyl esters, but also those of higher alcohols such as n-propanol, iso-propanol, n-butanol, isobutanol, tert - Butanol, n-pentanol, n-hexanol derived mono- di- and triesters, also mono-, di- or Trivinylester

and mixed methyl ethyl esters.

In the context of the present invention, it is also possible to use a mixture of a tri- or polycarboxylic acid and one or more of its derivatives. Likewise, it is within the scope of the present invention to provide a mixture of several various derivatives of one or more tri- or polycarboxylic acids to obtain component B2).

Examples of diols used for variant (b) of the present invention are ethylene glycol, propane-1,2-diol, propane-1,3-diol, butane-1,2-diol, butane-1,3-diol, butane-1 , 4-diol, butane-2,3-diol, pentane-1, 2-diol, pentane-1, 3-diol, pentane-1, 4-diol, pentane-1, 5-diol, pentane-2,3 -diol, pentane-2,4-diol, hexane-1, 2-diol, hexane-1, 3-dioI, hexane-1, 4-diol, hexane-1, 5-diol, hexane-1, 6-diol , Hexane-2,5-diol, heptane-1, 2-diol 1, 7-heptanediol, 1, 8-octanediol, 1, 2-octanediol, 1, 9-nonanediol, 1, 10-decanediol, 1, 2 Decanediol, 1,12-dodecanediol, 1,2-dodecanediol, 1,5-hexadiene-3,4-diol, cyclopentanediols, cyclohexanediols, inositol and derivatives, (2) -methyl-2,4-pentanediol, 2, 4-dimethyl-2,4-pentanediol, 2-ethyl-1,3-hexanediol, 2,5-dimethyl-2,5-hexanediol, 2,2,4-trimethyl-1,3-pentanediol, pinacol, diethylene glycol, Triethylene glycol, dipropylene glycol, tripropylene glycol, polyethylene glycols, HO (CH ₂ CH ₂ O) _n -H or polypropylene glycols HO (CH [CH ₃ ] CH ₂ O) _n -H or mixtures of two or more vert Retern the above compounds, wherein n is an integer and n = 4 to 25. One or both hydroxyl groups in the abovementioned diols can also be substituted by SH groups. Preference is given to ethylene glycol, propane-1,2-diol and diethylene glycol, triethylene glycol, dipropylene glycol and tripropylene glycol.

The molar ratio of molecules A to molecules B in the A _x B _y polyester in variants (a) and (b) is 4: 1 to 1: 4, in particular 2: 1 to 1: 2.

The at least trifunctional alcohols reacted according to variant (a) of the process may each have hydroxyl groups of the same reactivity. Also preferred here are at least trifunctional alcohols whose OH groups are initially identically reactive, but in which a drop in reactivity due to steric or electronic influences can be induced in the remaining OH groups by reaction with at least one acid group. This is the case, for example, when using methylolpropane or pentaerythritol.

However, the at least trifunctional alcohols reacted according to variant (a) can also have hydroxyl groups with at least two chemically different reactivities.

The differential reactivity of the functional groups may be due to either chemical (e.g., primary / secondary / tertiary OH group) or stubborn causes.

For example, the triol may be a triol having primary and secondary hydroxyl groups, preferred example being glycerin. When carrying out the reaction according to variant (a) according to the invention, preference is given to working in the absence of diols and monofunctional alcohols.

In carrying out the reaction according to variant (b) according to the invention, preference is given to working in the absence of mono- or dicarboxylic acids.

The process according to the invention is carried out in the presence of a solvent. Suitable are, for example, hydrocarbons such as paraffins or aromatics. Particularly suitable paraffins are n-heptane and cyclohexane. Particularly suitable aromatics are toluene, ortho-xylene, meta-xylene, para-xylene, xylene as a mixture of isomers, ethylbenzene, chlorobenzene and ortho- and meta-dichlorobenzene. Furthermore, as solvents in the absence of acidic catalysts are particularly suitable: ethers such as dioxane or tetrahydrofuran and ketones such as methyl ethyl ketone and methyl isobutyl ketone.

The amount of solvent added is according to the invention at least 0.1 wt .-%, based on the mass of the starting materials to be reacted, preferably at least 1 wt .-% and particularly preferably at least 10 wt .-%. It is also possible to use excesses of solvent, based on the mass of reacted starting materials to be used, for example the

1, 01- to 10-fold. Solvent amounts of more than 100 times, based on the mass of reacted starting materials to be reacted, are not advantageous because significantly lower concentrations of the reactants, the reaction rate decreases significantly, resulting in uneconomical long reaction times.

To carry out the process preferred according to the invention, it is possible to work as an additive in the presence of a dehydrating agent which is added at the beginning of the reaction. Suitable examples are molecular sieves, in particular molecular sieve 4Ä, MgSO ₄ and Na SOSO, *. It is also possible during the reaction to add further de-watering agent or to replace de-watering agent with fresh de-watering agent. It is also possible to distill off water or alcohol formed during the reaction and to use, for example, a water separator.

The process can be carried out in the absence of acidic catalysts. Preferably, one works in the presence of an acidic inorganic, organometallic or organic catalyst or mixtures of several acidic inorganic, organometallic or organic catalysts.

Examples of acidic inorganic catalysts for the purposes of the present invention are sulfuric acid, phosphoric acid, phosphonic acid, hypophosphorous acid, Aluminum sulphate hydrate, alum, acidic silica gel (pH = 6, especially = 5) and acidic alumina. Furthermore, for example, aluminum compounds of the general formula AI (OR) 3 and titanates of the general formula Ti (OR) ₄ can be used as acidic inorganic catalysts, where the radicals R can be identical or different and are selected independently of one another

C 1 -C 10 -alkyl radicals, for example methyl, ethyl, n-propyl, isopropyl, n-butyl, isobutyl, sec-butyl, tert-butyl, n-pentyl, isopentyl, sec-pentyl, neo-pentyl, 1, 2-dimethylpropyl, iso-amyl, n-hexyl, iso-hexyl, sec-hexyl, n-heptyl, iso-heptyl, n-octyl, 2-ethylhexyl, n-nonyl or n- decyl,

C 3 -C 12 -cycloalkyl radicals, for example cyclopropyl, cyclobutyl, cyclopentyl, cyclohexyl, cycloheptyl, cyclooctyl, cyclononyl, cyclodecyl, cycloundecyl and cyclododecyl; preferred are cyclopentyl, cyclohexyl and cycloheptyl.

The radicals R in Al (OR) 3 or Ti (OR) ₄ are preferably identical and selected from isopropyl or 2-ethylhexyl.

Preferred acidic organometallic catalysts are, for example, selected from dialkyltin oxides RaSnO, wherein R is as defined above. A particularly preferred representative of acidic organometallic catalysts is di-n-butyltin oxide, which is commercially available as so-called oxo-tin, or di-n-butyltin dilaurate.

Preferred acidic organic catalysts are acidic organic compounds with, for example, phosphate groups, sulfonic acid groups, sulfate groups or phosphonic acid groups. Particularly preferred are sulfonic acids such as para-toluene sulfonic acid. It is also possible to use acidic ion exchangers as acidic organic catalysts, for example polystyrene resins containing sulfonic acid groups, which are crosslinked with about 2% by mole of divinylbenzene.

It is also possible to use combinations of two or more of the aforementioned catalysts. It is also possible to use such organic or organometallic or even inorganic catalysts which are present in the form of discrete molecules in immobilized form.

If it is desired to use acidic inorganic, organometallic or organic catalysts, according to the invention 0.1 to 10% by weight, preferably 0.2 to 2% by weight, of catalyst is used.

The process according to the invention is carried out under an inert gas atmosphere, that is to say, for example, under carbon dioxide, nitrogen or noble gas, of which in particular argon can be mentioned. The inventive method is carried out at temperatures of 60 to 200 ⁰ C. Preferably, one works at temperatures of 130 to 180, in particular to 15O ⁰ C or below. Particularly preferred are maximum temperatures up to 145 ⁰ C, most preferably to 135 ° C.

The pressure conditions of the method according to the invention are not critical per se. You can work at significantly reduced pressure, for example at 10 to 500 mbar. The process according to the invention can also be carried out at pressures above 500 mbar. For reasons of simplicity, the reaction is preferably at atmospheric pressure; but it is also possible to carry out at slightly elevated pressure, for example up to 1200 mbar. You can also work under significantly elevated pressure, for example, at pressures up to 10 bar. The reaction is preferably at atmospheric pressure.

The reaction time of the process according to the invention is usually 10 minutes to 25 hours, preferably 30 minutes to 10 hours and particularly preferably one to 8 hours.

After completion of the reaction, the highly functional hyperbranched polyester can be easily isolated, for example by filtering off the catalyst and concentration, wherein the concentration is usually carried out at reduced pressure. Further suitable work-up methods are precipitation after addition of water and subsequent washing and drying.

Furthermore, component B2) can be prepared in the presence of enzymes or decomposition products of enzymes (according to DE-A 101 63163). The dicarboxylic acids reacted according to the invention do not belong to the acidic organic catalysts in the sense of the present invention.

Preference is given to the use of lipases or esterases. Highly suitable lipases and esterases are Candida cylindracea, Candida lipolytica, Candida rugosa, Candida antarctica, Candida utilis, Chromobacterium viscosum, Geotrichum viscosum, Geotrichum candidum, Mucor javanicus, Mucor mihei, pig pancreas, Pseudomonas spp., Pseudomonas fluorescens, Pseudomonas cepacia, Rhizopus arrhizus, Rhizopus delemar, Rhizopus niveus, Rhizopus oryzae, Aspergillus niger, Penicillium roquefortii, Penicillium camembertii or Esterase from Bacillus spp. and Bacillus thermoglucosidase. Particularly preferred is Candida antarctica lipase B. The enzymes listed are commercially available, for example from Novozymes Biotech Inc., Denmark.

The enzyme is preferably used in immobilized form, for example on silica gel or Lewatit®. Methods for the immobilization of enzymes are known per se, for example from Kurt Faber, "Biotransformations in organic chemistry", 3rd edition 1997, Springer Verlag, Chapter 3.2 "Immobilization" page 345-356. Immobilized enzymes are commercially available, for example from Novozymes Biotech Inc., Denmark.

The amount of immobilized enzyme used is 0.1 to 20 wt .-%, in particular 10 to 15 wt .-%, based on the mass of the total starting materials to be reacted.

The inventive process is carried out at temperatures above 6O ⁰ C. Preferably, one works at temperatures of 100 ⁰ C or below. Preference is given to temperatures up to 80 ° C., very particularly preferably from 62 to 75 ° C. and even more preferably from 65 to 75 ° C.

The process according to the invention is carried out in the presence of a solvent. Suitable are, for example, hydrocarbons such as paraffins or aromatics. Particularly suitable paraffins are n-heptane and cyclohexane. Particularly suitable aromatics are toluene, ortho-xylene, meta-xylene, para-xylene, xylene as a mixture of isomers, ethylbenzene, chlorobenzene and ortho- and meta-dichlorobenzene. Furthermore, very particularly suitable are ethers such as dioxane or tetrahydrofuran and ketones such as, for example, methyl ethyl ketone and methyl isobutyl ketone.

The amount of solvent added is at least 5 parts by weight, based on the mass of the starting materials to be reacted, preferably at least 50 parts by weight and more preferably at least 100 parts by weight. Levels of more than 10,000 parts by weight of solvent are not desirable because at significantly lower concentrations, the reaction rate decreases significantly, resulting in uneconomical long reaction times.

The process according to the invention is carried out at pressures above 500 mbar. Preferably, the reaction is at atmospheric pressure or slightly elevated pressure, for example up to 1200 mbar. You can also work under significantly elevated pressure, for example, at pressures up to 10 bar. The reaction is preferably at atmospheric pressure.

The reaction time of the method according to the invention is usually 4 hours to 6 days, preferably 5 hours to 5 days and more preferably 8 hours to 4 days.

After completion of the reaction, the highly functional hyperbranched polyester can be isolated, for example by filtering off the enzyme and concentration, wherein the concentration is usually carried out at reduced pressure. Other well suited Work-up methods are precipitation after addition of water followed by washing and drying.

The high-functionality, hyperbranched polyesters obtainable by the process according to the invention are distinguished by particularly low levels of discoloration and resinification. For the definition of hyperbranched polymers, see also: PJ. Flory, J. Am. Chem. Soc. 1952, 74, 2718 and A. Sunder et al., Chem. Eur. J. 2000, 6, No.1, 1-8. However, in the context of the present invention, "highly functional hyperbranched" means that the degree of branching, that is to say the average number of dendritic linkages plus the average number of end groups per molecule, is 10 - 99.9%, preferably 20 - 99%, more preferably 30-90% (see H. Frey et al., Acta Polym., 1997, 48, 30).

The polyesters according to the invention have a molecular weight M _w of 500 to

50 000 g / mol, preferably 1000 to 20 000, more preferably 1000 to 19 000. The polydispersity is 1, 2 to 50, preferably 1, 4 to 40, more preferably 1, 5 to 30 and most preferably 1, 5 bis 10. They are usually well soluble, ie Clear solutions with up to 50% by weight, in some cases even up to 80% by weight, of the polyesters according to the invention in tetrahydrofuran (THF), n-butyl acetate, ethanol and numerous other solvents can be prepared without the naked eye Gel particles are detectable.

The high-functionality hyperbranched polyesters according to the invention are carboxy-terminated, carboxy- and hydroxyl-terminated and are preferably terminated by hydroxyl groups.

The ratios of components B1) to B2) are preferably from 1:20 to 20: 1, in particular from 1:15 to 15: 1 and very particularly from 1: 5 to 5: 1, when used in a mixture.

The hyperbranched polycarbonates B1) / polyesters B2) used are particles with a size of 20-500 nm. These nanoparticles are finely distributed in the polymer blend, and the size of the particles in the compound is from 20 to 500 nm, preferably 50-50 nm. 300 nm.

Such compounds are commercially available e.g. available as Ultradur® high speed.

As component C), the molding compositions of the invention comprise 1 to 30, preferably 2 to 25 and in particular 5 to 20 wt .-% of a Flammschutzmittelkombinati- on C1) from 20 to 99, preferably from 50 to 85,% by weight of a halogen-containing flame retardant,

C2) 1 to 80 wt .-%, preferably 15 to 50 wt .-% of an antimony oxide.

Preferred oxides C2) are antimony trioxide and antimony pentoxide. For better dispersion, the oxide C2) can be incorporated into the polymer A) in so-called batches (concentrates), it being possible for example to use polymers in the concentrate which correspond to component A) or are different from the respective component A). Preference is given to concentrates of C2) in polyolefins, preferably polyethylene.

Suitable flame retardants C1) are preferably brominated epoxy resins, such as DER 511 or DER 542 from Dow Chemical Comp, having a bromine content of 46 to 51% and an epoxy content (mmol / kg) of 2820 to 3280 according to ASTM D-1652 or Sumiepoxy ESB 340 , 400, 500 and 700 from Sumitomo Chemical Comp, with M _w 400 to 4000 or PURASAMU EP 100 from Dainippon Ink & Chem. Inc., and brominated epoxy oligomers E 5119, E 5114 and 5112 from Shell Chemicals having the general formula as listed below but with n = 0.6 to 1.7.

A particularly preferred epoxy resin is

with n = 4 to 50, preferably 20 to 35 and in particular 26 to 33.

Such a resin is commercially available under the name CXB-2000H from Woojin Copolymers, KR. The bromine content is generally at least 45%, preferably at least 50%, in the molding compositions usually from 2 to 20, preferably from 4 to 12 wt .-%.

As component D), the molding compositions according to the invention 0 to 60, in particular up to 50% by weight may contain further additives and processing aids.

As component D), the molding compositions according to the invention 0 to 5, preferably 0.05 to 3 and in particular 0.1 to 2 wt .-% of at least one ester or amide of saturated or unsaturated aliphatic carboxylic acids having 10 to 40, preferably 16 to 22 carbon atoms with aliphatic saturated alcohols or amines having 2 to 40, preferably 2 to 6 carbon atoms.

The carboxylic acids can be 1- or 2-valent. Examples which may be mentioned are pelargonic acid, palmitic acid, lauric acid, margaric acid, dodecanedioic acid, behenic acid and particularly preferably stearic acid, capric acid and montanic acid (mixture of fatty acids having 30 to 40 carbon atoms).

The aliphatic alcohols can be 1 to 4 valent. Examples of alcohols are n-butanol, n-octanol, stearyl alcohol, ethylene glycol, propylene glycol, neopentyl glycol, pentaerythritol, with glycerol and pentaerythritol being preferred.

The aliphatic amines can be monohydric to trihydric. Examples of these are stearylamine, ethylenediamine, propylenediamine, hexamethylenediamine, di (6-aminohexyl) amine, with ethylenediamine and hexamethylenediamine being particularly preferred. Correspondingly, preferred esters or amides are glycerol distearate, glycerol tristearate, ethylenediamine distearate, glycerol monopalmitate, glycerol trilaurate, glycerol monobehenate and pentaerythritol tetrastearate.

It is also possible to use mixtures of different esters or amides or esters with amides in combination, the mixing ratio being arbitrary.

Other conventional additives D) are, for example, in amounts of up to 40, preferably up to 30 wt .-% rubber-elastic polymers (often also referred to as impact modifiers, elastomers or rubbers).

In general, these are copolymers which are preferably composed of at least two of the following monomers: ethylene, propylene, butadiene, isobutene, isoprene, chloroprene, vinyl acetate, styrene, acrylonitrile and acrylic or methacrylic esters with 1 to 18 C Atoms in the alcohol component.

Such polymers are e.g. in Houben-Weyl, Methods of Organic Chemistry, Vol. 14/1 (Georg Thieme Verlag, Stuttgart, 1961). Pages 392 to 406 and in the monograph of CB. Bucknall, "Toughened Plastics" (Applied Science Publishers, London, 1977).

In the following some preferred types of such elastomers are presented.

Preferred types of such elastomers are the so-called ethylene-propylene (EPM) and ethylene-propylene-diene (EPDM) rubbers. EPM rubbers generally have practically no double bonds, while EPDM rubbers can have 1 to 20 double bonds / 100 carbon atoms.

As diene monomers for EPDM rubbers, for example, conjugated dienes such as isoprene and butadiene, non-conjugated dienes having 5 to 25 carbon atoms such as penta-1, 4-diene, hexa-1, 4-diene, hexa-1, 5 -diene, 2,5-dimethylhexa-1, 5-diene and octa-1,4-diene, cyclic dienes such as cyclopentadiene, cyclohexadienes, cyclooctadienes and dicyclopentadienes and also alkenylnorbornenes such as 5-ethylidene-2-norbornene, Butylidene-2-norbornene, 2-methallyl-5-norbornene, 2-isopropenyl-5-norbornene and tricyclodienes such as 3-methyltricyclo (5.2.1.0.2.6) -3,8-decadiene or mixtures thereof. Preference is given to hexa-1, 5-diene, 5-ethylidene-norbornene and dicyclopentadiene. The diene content of the EPDM rubbers is preferably 0.5 to 50, in particular 1 to 8 wt .-%, based on the total weight of the rubber.

EPM or EPDM rubbers may preferably also be grafted with reactive carboxylic acids or their derivatives. Here are e.g. Acrylic acid, methacrylic acid and its derivatives, e.g. Glycidyl (meth) acrylate, as well as maleic anhydride.

Another group of preferred rubbers are copolymers of ethylene with acrylic acid and / or methacrylic acid and / or the esters of these acids. In addition, the rubbers may still contain dicarboxylic acids such as maleic acid and fumaric acid or derivatives of these acids, e.g. Esters and anhydrides, and / or monomers containing epoxy groups. These dicarboxylic acid derivatives or monomers containing epoxy groups are preferably incorporated into the rubber by addition of monomers containing dicarboxylic acid or epoxy groups of the general formulas I or II or III or IV to the monomer mixture

R ¹ C (COOR ² ) = C (COOR ³ ) R ⁴ (I)

R ^ R ⁴ rr

(H)

OC. .CO

CH ₀ = CR ⁹ - COO (CH 2 ₂ ) ', P-CH-CHR ⁸ (IV)

\ / O wherein R ¹ to R ^{9 represent} hydrogen or alkyl groups having 1 to 6 carbon atoms and m is an integer of 0 to 20, g is an integer of 0 to 10 and p is an integer of 0 to 5

The radicals R ¹ to R ⁹ preferably denote hydrogen, where m is 0 or 1 and g is 1. The corresponding compounds are maleic acid, fumaric acid, maleic anhydride, allyl glycidyl ether and vinyl glycidyl ether.

Preferred compounds of the formulas I, II and IV are maleic acid, maleic anhydride and epoxy groups-containing esters of acrylic acid and / or methacrylic acid, such as glycidyl acrylate, glycidyl methacrylate and the esters with tertiary alcohols, such as t-butyl acrylate. Although the latter have no free carboxyl groups, but in their behavior close to the free acids and are therefore as monomers with latent

Carboxyl groups called.

Advantageously, the copolymers consist of 50 to 98 wt .-% of ethylene, 0.1 to 20 wt .-% of monomers containing epoxy groups and / or methacrylic acid and / or monomers containing acid anhydride groups and the remaining amount of (meth) acrylic acid esters.

Particularly preferred are copolymers of

50 to 98, in particular 55 to 95 wt .-% ethylene,

0.1 to 40, in particular 0.3 to 20 wt .-% glycidyl acrylate and / or glycidyl methacrylate, (meth) acrylic acid and / or maleic anhydride, and

1 to 45, in particular 10 to 40 wt .-% n-butyl acrylate and / or 2-ethylhexyl acrylate.

Further preferred esters of acrylic and / or methacrylic acid are the methyl, ethyl, propyl and i- or t-butyl esters.

In addition, vinyl esters and vinyl ethers can also be used as comonomers.

The ethylene copolymers described above can be prepared by methods known per se, preferably by random copolymerization under high pressure and elevated temperature. Corresponding methods are generally known.

Preferred elastomers are also emulsion polymers whose preparation is described, for example, in Blackley in the monograph "Emulsion Polymerization". The emulsifiers and catalysts which can be used are known per se. Basically, homogeneously constructed elastomers or those with a shell structure can be used. The shell-like structure is determined by the order of addition of the individual monomers; the morphology of the polymers is also influenced by this order of addition.

By way of example, as monomers for the preparation of the rubber portion of the elastomers, acrylates such as e.g. N-butyl acrylate and 2-ethylhexyl acrylate, corresponding methacrylates, butadiene and isoprene and their mixtures called. These monomers can be reacted with other monomers such as e.g. Styrene, acrylonitrile, vinyl ethers and other acrylates or methacrylates such as methyl methacrylate, methyl acrylate, ethyl acrylate and propyl acrylate are copolymerized.

The soft or rubber phase (with a glass transition temperature below ⁰ ° C.) of the elastomers can be the core, the outer shell or a middle shell (in the case of elastomers with a more than two-shell structure); in the case of multi-shell elastomers, it is also possible for a plurality of shells to consist of a rubber phase.

In addition to the rubber phase, one or more hard components (with glass transition temperatures of more than 2O ⁰ C) on the structure of the elastomer involved, these are generally prepared by polymerization of styrene, acrylonitrile, methacrylonitrile, α-methylstyrene, p-methylstyrene , Acrylsäureestem and Methacrylsäureestem such as methyl acrylate, ethyl acrylate and methyl methacrylate produced as major monomers. In addition, smaller proportions of other comonomers can also be used here.

In some cases it has proven to be advantageous to use emulsion polymers which have reactive groups on the surface. Such groups are e.g. Epoxy, carboxyl, latent carboxyl, amino or amide groups, and functional groups obtained by concomitant use of monomers of the general formula

R ¹⁰ R ¹¹ C ^ H ₁ , ^ r ^ ^ YM IN rwof \ ¹²

O

can be introduced

where the substituents may have the following meanings:

R ^{10 is} hydrogen or a C 1 -C 6 -alkyl group, R ^{11 is} hydrogen, a C 1 - to C 5 -alkyl group or an aryl group, in particular phenyl,

R ^{12 is} hydrogen, a C 1 to C 10 alkyl, a C 6 to C 12 aryl group or -OR ¹³

R ^{13 is} a C 1 - to C 6 -alkyl or C 12- to C 12 -aryl group which may optionally be substituted by O- or N-containing groups,

X is a chemical bond, a C 1 - to C 10 -alkylene or C 6 -C 12 -arylene group or

O v T

Y O-Z or NH-Z and

Z is a C 1 -C 10 -alkylene or C $ -C12-arylene group.

The graft monomers described in EP-A 208 187 are also suitable for introducing reactive groups on the surface.

As further examples are acrylamide, methacrylamide and substituted esters of acrylic acid or methacrylic acid such as (Nt-butylamino) ethyl methacrylate, (N ₁ N-dimethylamino) ethyl acrylate, (N, N-dimethylamino) methyl acrylate and (N, N-diethylamino) called ethyl acrylate.

Furthermore, the particles of the rubber phase can also be crosslinked. Examples of monomers acting as crosslinkers are buta-1,3-diene, divinylbenzene, diallyl phthalate and dihydrodicyclopentadienyl acrylate, and also the compounds described in EP-A 50 265.

Furthermore, so-called graft-linking monomers can also be used, ie monomers having two or more polymerizable double bonds which react at different rates during the polymerization. Preference is given to using those compounds in which at least one reactive group polymerizes at about the same rate as the other monomers, while the other reactive group (or reactive groups), for example, polymerizes (polymerizes) much more slowly. The different polymerization rates bring a certain proportion of unsaturated double bonds in the rubber with it. If a further phase is subsequently grafted onto such a rubber, the double bonds present in the rubber react at least partially with the graft monomers to form chemical binders. fertilize, ie the grafted phase is at least partially linked by chemical bonds with the graft.

Examples of such graft-crosslinking monomers are allyl-containing monomers, in particular allyl esters of ethylenically unsaturated carboxylic acids, such as allyl acrylate, allyl methacrylate, diallyl maleate, diallyl fumarate, diallyl itaconate or the corresponding monoallyl compounds of these dicarboxylic acids. In addition, there are a variety of other suitable graft-linking monomers; for further details, reference is made here, for example, to US Pat. No. 4,148,846.

In general, the proportion of these crosslinking monomers in the impact-modifying polymer is up to 5% by weight, preferably not more than 3% by weight, based on the impact-modifying polymer.

In the following, some preferred emulsion polymers are listed. First, graft polymers having a core and at least one outer shell, which have the following structure:

These graft polymers, in particular ABS and / or ASA polymers in amounts of up to 40% by weight, are preferably used for the toughening of PBT, optionally mixed with up to 40% by weight of polyethylene terephthalate. Corresponding blend products are available under the trademark Ultradur®S (formerly Ultrablend® of BASF AG). Instead of graft polymers having a multi-shell structure, it is also possible to use homogeneous, ie single-shell, elastomers of buta-1,3-diene, isoprene and n-butyl acrylate or copolymers thereof. These products can also be prepared by concomitant use of crosslinking monomers or monomers having reactive groups.

Examples of preferred emulsion polymers are n-butyl acrylate / (meth) acrylic acid copolymers, n-butyl acrylate / glycidyl acrylate or n-butyl acrylate / glycidyl methacrylate copolymers, graft polymers having an inner core of n-butyl acrylate or butadiene-based and an outer shell of the above copolymers and copolymers of ethylene with comonomers which provide reactive groups.

The described elastomers may also be prepared by other conventional methods, e.g. by suspension polymerization.

Silicone rubbers, as described in DE-A 37 25 576, EP-A 235 690, DE-A 38 00 603 and EP-A 319 290, are likewise preferred.

Of course, it is also possible to use mixtures of the abovementioned rubber types.

Fibrous or particulate fillers D) which may be mentioned are carbon fibers, glass fibers, glass spheres, amorphous silica, asbestos, calcium silicate, calcium metasilicate, magnesium carbonate, kaolin, chalk, powdered quartz, mica, barium sulfate and feldspar, which may be present in quantities of up to 50 Wt .-%, in particular up to 40% are used.

Preferred fibrous fillers are carbon fibers, aramid fibers and potassium titanate fibers, glass fibers being particularly preferred as E glass. These can be used as rovings or cut glass in the commercial forms.

Mixtures of glass fibers D) with component B) in the ratio of 1: 100 to 1: 2 and preferably from 1:10 to 1: 3 are particularly preferred.

The fibrous fillers can be surface-pretreated for better compatibility with the thermoplastic with a silane compound.

Suitable silane compounds are those of the general formula

(X- (CH2) π) k-Si- (OC _m H2m ₊ i) 4-k

in which the substituents have the following meanings: X is NH ₂ -, CH ₂ -CH-, HO-,

\ /

O n is an integer from 2 to 10, preferably 3 to 4 m, an integer from 1 to 5, preferably 1 to 2 k, an integer from 1 to 3, preferably 1

Preferred silane compounds are aminopropyltrimethoxysilane, aminobutyltrimethoxysilane, aminopropyltriethoxysilane, aminobutyltriethoxysilane and the corresponding silanes which contain a glycidyl group as substituent X.

The silane compounds are generally used in amounts of 0.05 to 5, preferably 0.5 to 1, 5 and in particular 0.8 to 1 wt .-% (based on D) for surface coating.

Also suitable are acicular mineral fillers.

In the context of the invention, the term "needle-shaped mineral fillers" is understood to mean a mineral filler with a pronounced, needle-like character. An example is acicular wollastonite. Preferably, the mineral has a UD (length diameter) ratio of 8: 1 to 35: 1, preferably 8: 1 to 11: 1. The mineral filler may optionally be pretreated with the silane compounds mentioned above; however, pretreatment is not essential.

Kaolin, calcined kaolin, wollastonite, talc and chalk are mentioned as further fillers.

As component D), the thermoplastic molding compositions of the invention may contain conventional processing aids such as stabilizers, antioxidants, agents against thermal decomposition and decomposition by ultraviolet light, lubricants and mold release agents, colorants such as dyes and pigments, nucleating agents, plasticizers, etc.

Examples of antioxidants and heat stabilizers sterically hindered phenols and / or phosphites, hydroquinones, aromatic secondary amines such as diphenylamines, various substituted representatives of these groups and mixtures thereof in concentrations up to 1 wt .-%, based on the weight of the thermoplastic molding compositions mentioned. As UV stabilizers, which are generally used in amounts of up to 2 wt .-%, based on the molding composition, various substituted resorcinols, salicylates, benzothazoles and benzophenones may be mentioned.

It is possible to add inorganic pigments, such as titanium dioxide, ultramarine blue, iron oxide and carbon black, furthermore organic pigments, such as phthalocyanines, quinacridones, perylenes and also dyes, such as nigrosine and anthraquinones, as colorants,

The nucleating agents used may be sodium phenylphosphinate, aluminum oxide, silicon dioxide and preferably talc.

Other lubricants and mold release agents are usually used in amounts of up to 1 wt .-%. Preferred are long-chain fatty acids (e.g., stearic acid or behenic acid), their salts (e.g., Ca or Zn stearate), or montan waxes (mixtures of straight-chain, saturated carboxylic acids having chain lengths of 28 to

32 C atoms) as well as Ca or Na montanate as well as low molecular weight polyethylene or polypropylene waxes.

Examples of plasticizers are dioctyl phthalate, dibenzyl phthalate, butyl benzyl phthalate, hydrocarbon oils and N- (n-butyl) benzenesulfonamide.

The novel molding materials may contain from 0 to 2% by weight of fluorine-containing ethylene polymers. These are polymers of ethylene with a fluorine content of 55 to 76 wt .-%, preferably 70 to 76 wt .-%.

Examples of these are polytetrafluoroethylene (PTFE), tetrafluoroethylene-hexafluoropropylene copolymers or tetrafluoroethylene copolymers with smaller proportions (generally up to 50% by weight) of copolymerizable ethylenically unsaturated monomers. These are e.g. by Schildknecht in "Vinyl and Related Polymers", Wiley-Verlag, 1952, pages 484 to 494 and by Wall in "Fluoropolymers" (Wiley Interscience, 1972).

These fluorine-containing ethylene polymers are homogeneously distributed in the molding compositions and preferably have a particle size dso (number average) in the range of 0.05 to 10 .mu.m, in particular from 0.1 to 5 .mu.m. These small particle sizes can be achieved particularly preferably by using aqueous dispersions of fluorine-containing ethylene polymers and incorporating them into a polyester melt.

The thermoplastic molding compositions according to the invention can be prepared by processes known per se, in which the starting components in customary Mixing devices such as screw extruders, Brabender mills or Banbury mills are mixed and then extruded. After extrusion, the extrudate can be cooled and comminuted. It is also possible to premix individual components and then to add the remaining starting materials individually and / or likewise mixed. The mixing temperatures are usually 230 to 29O ⁰ C.

According to a further preferred procedure, the components B) and C) and optionally D) can be mixed with a prepolymer, formulated and granulated. The resulting granules are then condensed in solid phase under inert gas continuously or discontinuously at a temperature below the melting point of component A) to the desired viscosity.

The thermoplastic molding compositions according to the invention are characterized by good flowability combined with good mechanical properties and flameproofing properties.

In particular, the processing of the individual components (without clumping or caking) is possible without problems and in short cycle times, so that in particular thin-walled components come as an application in question, the mold covering is very low.

These are suitable for the production of fibers, films and moldings of any kind, in particular for applications as plugs, switches, housing parts, housing cover, headlight background (Bezel), shower head, Amaturen, irons, rotary switches, stove knobs, Friteusendeckel, door handles, (rear) mirror housing , (Rear) windscreen wiper, fiber optic sheathing.

Examples

Component A / 1:

Polybutylene terephthalate (PBT) with a viscosity number VZ of 130 ml / g and a carboxyl end group content of 34 mva / kg (Ultradur® B 4520 from BASF AG) (VZ measured in 0.5 wt .-% solution of phenol / o-dichlorobenzene, 1: 1 mixture) at 25 ^° C., containing 0.65% by weight of pentaerythritol tetrastearate (component D1 based on 100% by weight of A)

Component A / 2:

PBT as described under A / 1, but without D1. (Ultradur® B 4500 from BASF AG). Component A / 3:

PBT as described under A1, but with a VZ of 107 ml / g, (Ultradur® B 2550 from BASF AG).

Component B:

General procedure:

In a three-necked flask equipped with stirrer, reflux condenser and internal thermometer according to Table 1, the polyfunctional alcohol was mixed equimolar with diethyl carbonate and 250 ppm of catalyst (based on the amount of alcohol) was added. The mixture was then heated with stirring to 100 ⁰ C, in the experiment marked with * to 140 ⁰ C, and stirred for 2 h at this temperature. As the reaction progressed, the temperature of the reaction mixture was reduced due to the incipient boiling cooling of the liberated monoalcohol. Now, the reflux condenser was exchanged for a descending condenser, ethanol distilled off and the temperature of the reaction mixture slowly increased to 160 ° C.

The distilled ethanol was collected in a cooled round bottomed flask, weighed and the conversion percentage determined in relation to the theoretically possible full conversion (see Table 1).

The reaction products were then analyzed by gel permeation chromatography, eluent was dimethylacetamide, as a standard, polymethylmethacrylate (PMMA) was used.

Table 1 :

Distillate ethanol molecular quantity. on weight

Full turnover M _w Visk. 23 ° C OH number

Alcohol Catalyst [mol% 1 M _n Tm Pasl rmq KOH / αl

TMP x 1, 2 PO K ₂ CO ₃ 71 1920 9480 480

1293

TMP = trimethylolpropane

PO = propylene oxide Component C / 1:

n = 30

Component C / 2: antimony trioxide (as concentrate 90% in polyethylene).

Component D / 2: Glass fibers with an average thickness of 13 μm (epoxysilanized size).

Component D / 3: polytetrafluoroethylene (Teflon).

Component D / 4: Loxiol® EP 861 from Cognis GmbH: long-chain ester of pentaerythritol.

Production of molding compounds

The components A) to D) were mixed on a twin-screw extruder at 250 to 260 ° C and extruded in a water bath. After granulation and drying, specimens were sprayed and tested on an injection molding machine.

The granules were injection molded into shoulder bars according to ISO 527-2 and a tensile test was performed. In addition, impact strength was determined to ISO 179-2, viscosity (solvent for PBT according to DIN 53728 phenol / 1, 2-dichlorobenzene (1: 1) ISO 1628), MVR (ISO 1133) and the flow method tested, the flame retardance according to UL 94 certainly.

The compositions according to the invention and the results of the measurements can be taken from the tables. Table 2:

Table 3:

Table 4:

Claims

claims

Thermoplastic molding compositions containing

A) 10 to 99% by weight of at least one thermoplastic polymer,

B) 0 to 50% by weight

B1) at least one highly branched or hyperbranched polycarbonate having a

OH number from 1 to 600 mg KOH / g polycarbonate (according to DIN 53240,

Part 2), or B2) at least one hyperbranched or hyperbranched polyester of the type A _x B _y with x at least 1, 1 and y at least 2.1 or mixtures thereof

C) 1 to 30 wt .-% of a flame retardant combination, based on 100 wt .-% C),

C1) from 20 to 99% by weight of a halogen-containing epoxy resin, C2) from 1 to 80% by weight of an antimony oxide,

D) 0 to 60% by weight of other additives,

where the sum of the weight percent of components A) to D) is 100%.

Thermoplastic molding compositions according to claim 1, in which the component C1)

with n = 4 to 50 is constructed.

3. Thermoplastic molding compositions according to claims 1 or 2, containing 0.01 to 40 wt .-% B).

4. Thermoplastic molding compositions according to claims 1 to 3, in which the component B1) has a viscosity (mPas) at 23 ⁰ C (according to DIN 53019) of 50 to 200,000.

5. Thermoplastic molding compositions according to claims 1 to 4, in which the component B2) has a number average molecular weight M _n of 300 to 30,000 g / mol.

6. Thermoplastic molding compositions according to claims 1 to 5, in which the component B2) has a glass transition temperature T ₉ of -50 ⁰ C to 14O ⁰ C.

7. Thermoplastic molding compositions according to claims 1 to 6, in which the component B2) has an OH number (according to DIN 53240) of 0 to 600 mg KOH / g polyester.

8. Thermoplastic molding compositions according to claims 1 to 7, in which component B2) has a COOH number (according to DIN 53240) of 0 to 600 mg KOH / g

Polyester

9. Thermoplastic molding compositions according to claims 1 to 8, in which the component B2) has at least one OH number or COOH number greater than 0.

10. Thermoplastic molding compositions according to claims 1 to 9, in which the ratio of components B1): B2) is from 1:20 to 20: 1.

11. Thermoplastic molding compositions according to claims 1 to 10, in which the thermoplastic polymer is selected from the group of polyamides, polyesters, polycarbonates, vinylaromatic polymers, ASA, ABS, SAN polymers or mixtures thereof.

12. Thermoplastic molding compositions according to claims 1 to 11, in which the components A) is composed of polybutylene terephthalate, which is 0 to

50% by weight, based on 100% by weight of A), of polyesters other than polybutylene terephthalate.

13. Thermoplastic molding compositions according to claims 1 to 12, in which C2) is built up from antimony trioxide or antimony pentoxide or mixtures thereof.

14. Use of the thermoplastic molding compositions according to claims 1 to 13 for the production of fibers, films and moldings of any kind.

15. Fibers, films and moldings of any kind obtainable from the thermoplastic molding compositions according to claims 1 to 13.