EP1204648A1

EP1204648A1 - N-oxyl radicals

Info

Publication number: EP1204648A1
Application number: EP00960475A
Authority: EP
Inventors: Susanne Brinkmann-Rengel; Sylke Haremza; Heinz Friedrich Sutoris; David Christie; Roman Benedikt Raether; Jizhuang Cao
Original assignee: BASF SE
Current assignee: BASF SE
Priority date: 1999-08-18
Filing date: 2000-08-17
Publication date: 2002-05-15
Also published as: DE19939031A1; WO2001012614A1; US6639033B1

Abstract

The invention relates to N-oxyl radicals of formula (I) wherein X represents S, NR<5>, O, SO or SO2, and; R<1>, R<2>, R<3>, R<4>, and R<5>, independent of one another, represent organic groups or; R<1> and R<2> and/or R<3> and R<4>, together with the carbon atom that carries them, represent a ring comprised of at least 3 atoms. The N-oxyl radicals are suited for controlling radical polymerizations and for stabilizing ethylenically unsaturated monomers against unwanted polymerization.

Description

N-oxyl radicals

description

The present invention relates to N-oxyl radicals, N-oxyl radical formers and their use in the radical polymerization of ethylenically unsaturated monomers.

N-oxyl radicals and N-oxyl radical formers which are derived from a secondary A in which does not have any hydrogen atoms on the α-C atoms are known. They are or form extremely stable radicals and can usually be represented as pure substances.

Such stable N-oxyl radicals are used, inter alia, as inhibitors of undesired radical polymerizations (cf., for example, US Pat. No. 5,322,960). Another application of such stable N-oxyl radicals is that their presence enables a certain control of radical-initiated polymerizations of compounds (monomers) having at least one ethylenically unsaturated group (cf. e.g. EP-A 135280, US-A 5,412,047 and US-A 5,322,912).

Radically initiated polymerizations of monomers usually have the disadvantage that the molecular weight of the polymer chains does not increase linearly with the polymerization conversion and that the polymer chains of the resulting polymer generally do not have a uniform molecular weight. This means that the polymer obtainable by free-radically initiated polymerization is generally not monodisperse with regard to the "molecular weight" property, but normally has a related polydispersity index PDI of> 2 (PDI = M _w / M _n , with M _w = weight-average Molecular weight of the polymer and M _n = number average molecular weight of the polymer). Both of the aforementioned appearances are attributed to termination reactions as a result of an irreversible combination of growing free radical polymer chain ends.

The controlling influence of stable N-oxyl radicals (which are normally not able to initiate radical polymerisation of monomers) is probably due to the fact that the stable N-oxyl radicals do not have reactive radical ends of a growing polymer chain that are irreversibly termi-

US 4,528,370 relates to polysubstituted 2-morpholones. As far as nitroxyl compounds are addressed in this publication, only the preparation of the nitroxyls of precursor compounds in the form of substituted hydroxyethylaminoacetates is mentioned.

EP-A-0 869 137 discloses a polymerization process for the preparation of (meth) acrylates-containing homo- or block copolymers in the presence of certain nitroxyls of the piperazinone or morpholone structure type.

However, the known radical-initiated polymerization processes in the presence of nitroxyl radicals have the disadvantage that long reaction times are required to achieve practicable conversions.

DE-A-2 351 865 discloses, among other things, the compound 2,2,6,6-tetramethyl-l-aza-4-thiacyclohexane-1,4,4-trioxide. The use of this compound to control radical polymerizations is neither taught nor suggested.

The object of the present invention was therefore to provide new N-oxyl radicals or formers of new N-oxyl radicals, in the presence of which the controlled radical polymerization leads to higher conversions in a shorter time. They should also be suitable for carrying out controlled free-radical polymerizations of non-styrenic monomers, in particular of esters of acrylic and / or methacrylic acid.

According to the invention, this object is achieved by N-oxyl radicals of the general formula I

wherein X is S, NR ⁵ , O or SO and

R ¹ , R ² , R ³ , R ⁴ and R ⁵ independently of one another represent organic radicals or

R ¹ and R ² and / or R ³ and R ⁴ together with the carbon atom bearing them represent a ring consisting of at least 3 atoms. The object is also achieved by a process of free-radically initiated polymerization of ethylenically unsaturated monomers, which is characterized in that the polymerization is carried out in the presence of N-oxyl radicals of the formula I, where X can additionally stand for SO ₂ .

In a preferred embodiment, the N-oxyl radicals of the general formula I are formed by a spiro ring system, formed from R ¹ and R ² and / or R ³ and R ⁴ together with the carbon atom carrying them, particularly preferably from R ¹ and R ² together with the C atom carrying them. In the ring, two non-adjacent ring atoms can be bridged by a divalent organic radical and / or the ring can be fused to another ring. Advantageously, the ring formed from R ¹ and R ² or R ³ and R ⁴ together with the C atom carrying them consists of 3 to 10, preferably three, five, six or seven atoms, the free valences of the ring forming atoms with hydrogen and / or organic radicals, preferably C _{1 -C} 2 _alkyl groups, preferably C 1 -C 4 alkyl groups (e.g. the methyl, ethyl, n-propyl, iso-propyl, n- Butyl, iso-butyl and tert-butyl group) are saturated. Aryl groups can also be considered as such saturating residues. Among them, the phenyl and naphthyl groups are preferred. Normally the ring is a saturated ring and usually the ring-forming atoms are carbon atoms, but the ring-forming atoms can also be e.g. B. include one or two heteroatoms, such heteroatoms being primarily N, O and / or S.

The invention relates in particular to N-oxyl radicals of the general formula I, in which R ¹ , R ² , R ³ , R ⁴ and R ^{5 are,} independently of one another, C ₁ -C ₂ -alkyl, C ₅ -C ₈ cycloalkyl, C ₇ -C ₂ o-aralkyl, optionally substituted C ₆ -Cιo-aryl, heteroaryl,

- R6 - OR ⁷ -R ⁶ - 0 CH ₂ -CH-θ4-R ⁷ R ⁶ - 0 - C - R ⁸ n

(CH ₂ ) _k

I H

OO - R ⁶ - OSiR ⁸ ₃ , - R ⁹ - C - OR ¹⁰ , - R ⁹ - C -NR ⁷ ₂ or - R ⁹ - CN

stand in what

R ⁶ for optionally branched -C ₂₀ alkylene; R ⁷ each independently for H, -CC ₂₀ alkyl, optionally interrupted by oxygen atoms C ₃ -C ₂₀ cycloalkyl or aryl; R ⁸ each independently for C ₁ -C ₀ -alkyl or aryl; R ⁹ for a chemical bond or optionally branched -C-C ₀ alkylene; and R ^{10 is} H, C ₁ -C ₂₀ alkyl, aryl or an alkali metal; k for 0 or 1; and n represents an integer from 1 to 100,

or R ³ and R ⁴ together for an oxygen atom and / or R ¹ and R ² and / or R ³ and R ⁴ together with the C atom carrying them form a carbocyclic ring consisting of 3 to 10 atoms, in which 1 or 2 C atoms can be replaced by 0, S or N and / or in which two non-adjacent atoms can be bridged via a divalent organic radical, preferably Cχ-C ₃ alkylene, and / or that with another, preferably 5- or 6-membered ring can be fused.

If aryl radicals are substituted, the substituents include C _x - to C ₆ -alkyl, Cx to C ₆ -alkoxy, -S0 ₃ H, S0 ₃ M (where M is an alkali metal, e.g. Na or K) ) or N0 ₂ in consideration.

"Heteroaryl" preferably stands for heteroaromatic five-membered rings with 1, 2, 3 or 4 heteroatoms selected from O, S or N.

R ¹ and R ² and / or R ³ and R ⁴ together with the C atom z. B. form the following ring systems:

Particularly preferred N-oxyl radicals have the general formula II:

where X has the meaning already given,

R ³ and R ⁴ independently of one another are C 1 -C ₄ -alkyl, phenyl, naphthyl or an aromatic five-membered ring or R ³ and R ⁴ together stand for - (CH ₂ ) ₀ - and p and o independently of one another others represent an integer from 2 to 8, preferably 4 to 6.

The preparation of compounds I is possible via various synthesis steps known per se. As a rule, it takes place via a secondary amine, the

N- H group oxidatively into the corresponding N-oxyl group

N- O "is transferred.

Peroxides such as H ₂ O, t-butylhydroxyperoxide, cumene hydroperoxide, peracids such as metachloroperbenzoic acid, α-chloroperbenzoic acid, peracetic acid, p-nitrobenzoic acid, perbenzoic acid or magnesium monoperoxyphthalate are suitable as oxidizing agents. The oxidation can be carried out in an inert solvent such as CH ₂ C1 ₂ , petroleum ether, toluene, xylene or benzene.

The starting amine of Formula IV

where R ¹ , R ² , R ³ , R ⁴ and R ^{5 have} the meaning already given, z. B. can be obtained as follows (with X = O):

R ^l

R ₃ C = 0 + CHC1 ₃ R ₃ R ¹

R I I

H0-CH ₂ -C-NH ₂ HO-CH ₂ -C-NH-C-COOM I MOH I ι R ⁴ R ⁴ R ²

M = alkali metal, e.g. B. Na or K

A mono- or disubstituted 2-aminoethanol is used here with a cyclic ketone and a haloform, e.g. B. chloroform or bromoform, in the presence of an alkali metal hydroxide, optionally under phase transfer conditions, converted to a substituted alkali metal hydroxyethylaminoacetate. This can be cyclized under acid catalysis. With regard to the reaction conditions, reference is made to US Pat. No. 4,528,370.

The resulting amine can e.g. B. reduced with lithium aluminum hydride and converted into a diol.

Then the cyclization takes place under acid catalysis z. B, with methanesulfonic acid.

(IV)

With regard to the reaction conditions, reference is made to JT Lai, Synthesis 2 (1984) pp. 122-124. A ine of the formula IV, in which X is S, NR ⁵ , SO or S0 ₂ , can be prepared in an analogous manner from corresponding starting materials.

Instead of converting the amine directly into an N-oxyl radical according to the invention, it can also be subjected to a wide variety of modifications in a manner known per se in order to subsequently obtain N-oxyl radicals modified in a correspondingly oxidative manner (but of course it can the N-oxyl radical can also be modified as such).

The invention also relates to N-oxyl radical formers, which are characterized in that by ho olytic cleavage, for. B. by thermolysis, a chemical bond as a fragment of an N-oxyl radical according to the invention. They have the general formula III

wherein the symbols X, R ¹ , R ² , R ³ and R ^{4 have} the meaning already indicated and T stands for an organic radical with a molecular weight of 15 or more, preferably from 29 to 500,000. T stands for. B. for

Rll

- C - R ^l

R ^l3

wherein R ¹¹ , R ¹² and R ^{13 are} independently hydrogen, C _! -C -alkyl, phenyl, a cyano or ester group, or a polymer chain of units of ethylenically unsaturated monomers. The rest of CfR ¹¹ ) (R ¹² ) (R ¹³ ) is e.g. B. for methyl, ethyl, t-butyl, cyclohexyl, octyl, phenyl, C (CN) (CH ₃ ) ₂ , CHPhCH ₃ or CH (CH ₃ ) COOR, (R = z. B. Cχ-C ₄ alkyl ).

The N-oxyl radical formers III can be obtained by reacting N-oxyl radicals of the formula I with a radical initiator, optionally in the presence of ethylenically unsaturated monomers. N-oxyl radical formers III, in which T stands for a polymer chain, are in a simple manner, for. B. obtainable by radically polymerizing a small amount of monomers using a radical polymerization initiator (e.g. peroxide, hydroperoxide and / or azo compound) in the presence of an N-oxyl radical I and then cleaning the polymerization product by falling over (cf. e.g. DE-A 19735225). T can e.g. B. 1 to 100,000, preferably 3 to 50,000, comprise monomer units. As further processes for the preparation of N-oxyl radical formers according to the invention, those disclosed in US Pat. No. 5,021,481 can be used analogously.

The invention also relates to a process for the radical-initiated polymerization of ethylenically unsaturated monomers, which is characterized in that the polymerization takes place in the presence of N-oxyl radicals of the formula I. After he- Processes according to the invention can polymerize pure monomers or monomer mixtures.

The method according to the invention is usually carried out at elevated temperature, for. B. 50 to 200 ° C, preferably 60 to 180 ° C. To carry out the method, for. B. a mixture of (1) either (i) nitroxyl radical and optionally radical initiator or (ii) nitroxyl radical generator; and (2) heating at least one ethylenically unsaturated monomer. The reaction times are generally 30 minutes to 6 days, in particular 1 hour to 60 hours. By cooling, e.g. B. to room temperature, the reaction can be stopped or frozen. The polymer can then be isolated and optionally washed and dried.

Thermal initiation of the polymerization without the addition of a radical initiator is particularly suitable for the polymerization of styrene or styrene-containing monomer mixtures.

The process according to the invention is particularly suitable for the production of block copolymers. These are obtained by successively polymerizing different monomers or monomer mixtures of different compositions. For this purpose, the procedure is preferably such that at least one first monomer is polymerized in the presence of the N-oxyl radicals to obtain an intermediate polymer, the intermediate polymer is optionally isolated and at least one second monomer is polymerized in the presence of the intermediate polymer.

In particular, a method is preferred in which one

a) a mixture of (1) either (i) radical initiator and nitroxyl radical or (ii) nitroxyl radical generator; and (2) heated at least one first ethylenically unsaturated monomer to obtain an intermediate polymer,

b) optionally isolating the intermediate polymer,

c) to the intermediate polymer at least one of the first

Monomer different second ethylenically unsaturated monomer and heated the mixture to obtain a block copolymer, and

d) the block copolymer is isolated and, if appropriate, washed and dried. In order to obtain higher block copolymers, step c) can be repeated one or more times, a third or further monomer being used instead of the second ethylenically unsaturated monomer. Monomer mixtures can also be used instead of pure monomers. “Different monomers” are also understood to mean monomer mixtures of different compositions. The blocks of a block copolymer obtained according to the invention can accordingly represent homo- or copolymer blocks.

The isolation of the intermediate polymer is recommended when the highest possible purity, sharp block boundaries or high homogeneity within the blocks are desired. The isolation of the intermediate polymer prevents unreacted first monomer from being incorporated into the block of the second monomer that forms. Isolation of the intermediate polymer or the block copolymer can, for. B. done by failures.

The monomers polymerizable according to the invention include olefins, such as, for. B. ethylene, vinyl aromatic monomers such as styrene, α-methylstyrene, o-chlorostyrene or vinyltoluenes, 1,1- and 1,2-diphenylethylene, vinyl and vinylidene halides such as vinyl and vinylidene chloride, esters of vinyl alcohol and 1 to 12 C. -Atomic monocarboxylic acids such as vinyl acetate, vinyl propionate, vinyl n-butyrate, vinyl laurate and commercially available monomers VEOVA ^® 9 - 11 (VEOVA X is a trade name of Shell and stands for vinyl esters of carboxylic acids, which are also known as Versatic X acids are), esters of allyl alcohol and monocarboxylic acids having 1 to 12 carbon atoms such as allyl acetate, allyl propionate, allyl n-butyrate and allyl laurate, esters of α, β-monoethylenically unsaturated mono- and dicarboxylic acids preferably having 3 to 6 carbon atoms such as, in particular, acrylic acid, methacrylic acid, maleic acid, fumaric acid and itaconic acid, with alkanols which generally have 1 to 12, preferably 1 to 8 and in particular 1 to 4, carbon atoms, such as particularly Acrylic acid and methacrylic acid methyl, ethyl, n-butyl, isobutyl, tert-butyl and -2-ethylhexyl ester, dimethyl maleate or n-butyl maleate, nitriles α, β-monoethylenically unsaturated Carbon acids, such as acrylonitrile, and C _ ₈ -conjugated dienes, such as 1,3-butadiene and isoprene. But also 3 to 6 carbon atoms α, ß-monoethylenically unsaturated mono- and dicarboxylic acids and their aluides such as. B. acrylic acid, methacrylic acid, maleic acid, fumaric acid, itaconic acid, acrylamide and methacrylamide, N-methylacrylamide, N-ethylacrylamide, N-isopropylacrylamide and N, N'-

Dimethylacrylamide, also vinylsulfonic acid and its water-soluble salts and N-vinylpyrrolidone are suitable. This also applies for those monomers which usually increase the internal strength of the resulting polymers and which normally have an epoxy, hydroxyl or N-methylol group. Examples of these are N-alkylolamides of α, β-monoethylenically unsaturated carboxylic acids having 3 to 10 C atoms and their ethers with alkanols having 1 to 4 C atoms, among which the N-methylolacrylamide and the N-methylolmethacrylamide are very particularly preferred are.

In a preferred embodiment of the process according to the invention, vinylaromatic monomers, dienes or (meth) acrylic acid esters or mixtures thereof are used as monomers. In particular, the monomers used are selected from styrene, α-methylstyrene, vinyltoluene, diphenylethylene, acrylonitrile, butadiene, isoprene, n-butyl acrylate, methyl methacrylate or mixtures thereof.

In a further preferred embodiment of the process according to the invention, at least one vinylaromatic monomer, if appropriate in a mixture with other monomers, is polymerized.

In a further preferred embodiment of the process according to the invention, at least one diene, optionally in a mixture with other monomers, is polymerized.

In a further preferred embodiment of the process according to the invention, at least one (meth) acrylic acid ester, optionally in a mixture with other monomers, is polymerized.

The process according to the invention can be carried out as solution, substance, precipitation, suspension, emulsion, mini-emulsion and microemulsion polymerization or inverse radical emulsion polymerization. The polymerization can be carried out batchwise, semi-continuously or continuously.

In principle, all those which are capable of initiating a radical polymerization are suitable as radical polymerization initiators. It can be peroxides, hydroperoxides, peresters, percarbonates, persulfates, azo compounds or compounds with an unstable carbon-carbon bond. They can be both oil-soluble and water-soluble and are adapted to the chosen polymerization medium and the chosen polymerization temperature in a manner known per se. Redox initiator systems are also suitable. Specific examples of suitable initiators are hydrogen peroxide, tert-butyl hydroperoxide, di-tert-butyl peroxide, tert-amylhydroperoxide, dibenzoyl peroxide, potassium or sodium, ammonium peroxodisulfate, methyl ethyl ketone peroxide, dilauryl peroxide, cumyl hydroperoxide, dicumyl peroxide and azonitrile peroxide. Redox initiator systems include e.g. As sodium disulfite, sodium sulfite, ascorbic acid, iso-ascorbic acid, sodium formaldehyde sulfoxylate and the like in conjunction with suitable oxidizing agents, such as the initiators mentioned above.

The amount of radical initiator is preferably 10 ^-6 to 33 mol%, in particular 10 ^-4 to 10 mol%, based on the monomers.

Based on the molar amount of free radicals is monomers to be polymerized the kalen for a controlled radical polymerization to be used amount of the inventive N-oxyl radicalized or N-oxyl radical formers generally 10 ^{~ 4} to 33 mol .-%, usually 0.005 up to 20 mol%. The molar ratio between N-oxyl radicals and radical centers which arise when the polymerization initiator disintegrates is generally chosen to be 0.25 to 5, frequently 0.4 to 4, for a controlled radical-initiated polymerization.

The polymers prepared by the process according to the invention preferably have a molecular weight in the range from about 500 to about 500,000. The conversion of monomer to polymer can be up to 99% by weight.

In emulsion polymerization and its variants (microemulsion, miniemulsion), the monomers are emulsified in water, for which emulsifiers are used.

Suitable anionic, cationic and neutral (non-ionic) emulsifiers known to the person skilled in the art are suitable as emulsifiers. Anionic emulsifiers are e.g. B. alkali metal salts of higher fatty acids with 10 to 30 carbon atoms such as palmitic, stearic and oleic acid, alkali metal salts of sulfonic acids with z. B. 10 to 16 carbon atoms, especially sodium salts of alkyl or alkylarylsulfonic acids, alkali metal salts of half esters of phthalic acid, and alkali metal salts of resin acids such as abietic acid. Cationic emulsifiers are e.g. B. salts of long-chain, in particular unsaturated amines with 12 to 18 carbon atoms, or quaternary ammonium compounds with longer-chain olefin or paraffin residues (ie salts of quaternized fatty amines). Neutral emulsifiers are e.g. B. ethoxylated fatty alcohols, ethoxylated fatty acids or ethoxylated phenols and fatty acid esters of polyhydric alcohols such as Pentaerythritol or sorbitol. Initiators which are poorly soluble in the monomer but readily soluble in water are preferably used for the emulsion polymerization. Peroxosulfates such as potassium, sodium or ammonium peroxodisulfate are therefore preferably used, or redox systems.

Buffer substances such as Na ₂ HP0 ₄ / NaH ₂ P0 ₄ or Na citrate / citric acid can be used as further additives in the polymerization in order to set an essentially constant pH. Molecular weight regulators, for example mercaptans such as t-dodecyl mercaptan, or ethylhexyl thioglycolate can also be used. These further additives can be added continuously or discontinuously at the beginning and / or during the preparation of the emulsion and / or during the polymerization.

In mini-emulsion polymerization, an emulsion is prepared from the monomers, water and emulsifiers by allowing high shear forces to act. Homogenizers known to those skilled in the art are used for this, such as pressure homogenizers, devices with a rotor-stator system or colloid mills or ultrasound devices.

In suspension polymerization and its variants (microsuspension), the monomers are dispersed in water, for which protective colloids are also used. Suitable protective colloids are cellulose derivatives such as carboxymethyl cellulose and hydroxymethyl cellulose, poly-N-vinylpyrrolidone, polyvinyl alcohol and polyethylene oxide, anionic polymers such as polyacrylic acid and their copolymers and cationic polymers such as poly-N-vinylimidazole. The amount of this

Protective colloids are preferably 0.1 to 5% by weight, based on the total mass of the emulsion. Suitable protective colloids are described, for example, in Encyclopedia of Polymer Science and Engineering, Vol. 16, (1989) p. 448, published by J. Wiley.

In the case of precipitation polymerization, the monomers used are soluble in the continuous phase (eg solvent or solvent mixture), but the resulting polymers are insoluble or only soluble to a limited extent and therefore precipitate out during the polymerization. Bulk polymerizations in which the resulting polymer is insoluble in the monomer and therefore precipitate out are also possible.

In bulk or bulk polymerization, the monomers are polymerized without the addition of a reaction medium using the monomer-soluble initiators mentioned, ie the monomers are the reaction medium. It can also be initiated thermally.

In solution polymerization, an organic solvent such as toluene, cyclohexane, ethylbenzene or dimethyl sulfoxide is used or is also used to dilute the monomers.

The process according to the invention can also be carried out as a combined process in which at least two of the polymerization processes described above are combined with one another. Mass / solution, solution / precipitation, mass / suspension and mass / emulsion should be mentioned in particular, starting with the former and ending with the latter.

The N-oxyl radical, depending on its solubility behavior, either as such or dissolved in organic solvents such as alcohols, e.g. As methanol and / or ethanol, ethyl acetate, dimethylformamide, toluene, ethylbenzene, cyclohexane or benzene or mixtures thereof can be used. Also preferred is the addition of the N-oxyl radical in the form of a solution in a monomer or monomer mixture to be polymerized.

By adding inorganic or organic acids, such as 3-indole butyric acid, indolylacetic acid, or organic sulfonic acids, such as camphorsulfonic acid or p-toluenesulfonic acid (cf.

US-A-5,322, 912) or by adding dimethyl sulfoxide (cf. US-A-5,412, 047) or 2-fluoro-l-methylpyridinium-p-toluenesulfonate (cf. Macromolecules 28 (1995) 8453 ff) to the polymerization mixture the polymerization rate of the process according to the invention is generally increased.

The process according to the invention is usually carried out at an absolute pressure in the range from normal pressure to 60 bar, preferably up to 45 bar.

The polymers obtainable by the process according to the invention can be used as such or blended with other polymers and / or additives.

Such other polymers are in particular thermoplastic polymers. Such polymers include polyesters such as polyethylene terephthalate and polybutylene terephthalate, polycarbonates, polyamides, polyoxymethylene, polystyrene, polyolefins such as polyethylene and polypropylene, polyvinyl chloride and styrene copolymers such as polystyrene acrylonitrile. As additives come usual additives, such as. B. lubricants or mold release agents, pigments, dyes, flame retardants, antioxidants, light stabilizers, fibrous and powdery fillers or reinforcing agents or antistatic agents, as well as other additives, or mixtures thereof.

Suitable lubricants and mold release agents are e.g. B. fatty acids such as stearic acids, stearyl alcohol, fatty acid esters with 6 to 20 carbon atoms such. B. stearic acid esters, metal salts of fatty acids such as. B. Ca, Al, Zn stearate, fatty acid amides such as stearic acid amides, and silicone oils, montan waxes and those based on polyethylene and polypropylene, further hydrocarbon oils, paraffins and carboxylic acid esters from long-chain carboxylic acids and ethanol, fatty alcohols, glycerol , Ethanediol, pentaerythritol or other alcohols.

Pigments are, for example, titanium dioxide, phthalocyanines, ultramarine blue, iron oxides or carbon black, and the class of organic pigments.

Dyes are to be understood as all dyes which can be used for the transparent, semi-transparent or non-transparent coloring of polymers, in particular those which are suitable for coloring styrene copolymers. Dyes of this type are known to the person skilled in the art.

As flame retardants such. B. the halogen-containing or phosphorus-containing compounds known to the person skilled in the art, magnesium hydroxide, as well as other common compounds, or mixtures thereof can be used.

Suitable antioxidants (heat stabilizers) are, for example, sterically hindered phenols, hydroquinones, various substituted representatives of this group and mixtures thereof. They are commercially available as Topanol or Irganox.

Suitable light stabilizers are e.g. B. various substituted resorcinols, salicylates, benzotriazoles, cinnamic acid compounds, organic phosphites and phosphonites, benzophenones, HALS (hindered amine light stabilizers), such as z. B. are commercially available as Tinuvin.

Esters and / or amides of β- (3,5-di-tert-butyl-4-hydroxyphenyl) propionic acid and / or benzotriazoles can also be used as stabilizers. Possible antioxidants are mentioned by way of example in EP-A-698,637 and EP-A-669,367. In particular, 2, 6-di-tert-butyl-4-hy- can be used as phenolic antioxidants droxyphenyl propionate and N, N '-Di- (3, 5-di-tert-butyl-4-hydroxy-phenyl-propionyl) hexamethylene diamine.

Examples of fibrous or pulverulent fillers are carbon or glass fibers in the form of glass fabrics, glass mats or glass silk rovings, cut glass, glass balls and tungstenonite, particularly preferably glass fibers. If glass fibers are used, they can be equipped with a size and an adhesion promoter for better compatibility with the blend components. Glass fibers can be incorporated both in the form of short glass fibers and in the form of continuous fibers (rovings).

Suitable particulate fillers are carbon black, amorphous silica, magnesium carbonate (chalk), powdered quartz, mica, bentonite, talc, feldspar or in particular calcium silicates such as wollastonite and kaolin.

Suitable antistatic agents are, for example, amine derivatives such as N, N-bis (hydroxyalkyl) alkylamines or alkylene amines, polyethylene glycol esters and glycerol mono- and distearates, and mixtures thereof. The individual additives are used in the usual amounts. The additives are usually used in an amount of 0 to 50% by weight, based on the total of block copolymers and additives.

The mixing of the polymers produced according to the invention with the other polymers and / or additives takes place continuously or discontinuously according to mixing methods known per se, for example with melting in an extruder, Banbury mixer, kneader, roller mill or calender. However, the components can also be mixed "cold" and the mixture is only melted and homogenized during processing.

The mixtures obtained can be pelletized or granulated, for example, or processed by generally known methods, for example by extrusion, injection molding, foaming with blowing agents, or calendering.

The radicals and radical formers according to the invention are also suitable as inhibitors for preventing an undesired radical-initiated polymerization of monomers, ie for stabilizing monomers (as stabilizers). The invention therefore also relates to the use of the N-oxyl radicals according to the invention for stabilizing ethylenically unsaturated monomers against undesired radical-initiated polymerization. The Use concentrations for this are generally 0.001 to 0.1 mol%, based on the monomers.

The radicals and radical formers according to the invention are also suitable for stabilizing inanimate organic material against light and heat. Organic materials include z. B. cosmetic preparations such as ointments and lotions, pharmaceutical formulations, photographic recording materials, in particular photographic emulsions, intermediates for plastics and lacquers, but in particular plastics and lacquers themselves. The radicals or radical formers according to the invention can be used above all to stabilize plastics when they are processed or used. You will the plastics z. B. added during or before processing.

The invention is illustrated in more detail by the following examples.

Example 1: 8, 8-Dimethyl-10-oxa-7-aza-spiro [5.5] undecan-7-oxyl

MCPBA

22.6 g of 3-chloroperoxybenzoic acid are added in portions within 2 hours at 0 ° C. to 11.7 g of 3,3-pentamethylene-5,5-dimethyl-morpholine in 350 ml of methylene chloride. The mixture is then stirred for 12 hours, the temperature being raised to 23 ° C. Then 175 ml of saturated NaHC0 ₃ solution are added. The organic phase is separated, extracted with 150 ml of 20% Na ₂ S0 ₃ solution and three times with 150 ml of water. The organic phase is dried with MgS0, filtered and concentrated in vacuo. Yield: 12.3 g.

Example 2: 7, 7-Dimethyl-9-oxa-6-aza-spiro [4.5] decane-6-oxyl

19.6 g of 3-chloroperoxybenzoic acid are added in portions over 2 hours at 0 ° C. to 11.4 g of 3,3-tetramethylene-5,5-dimethyl-morpholine in 200 ml of methylene chloride. The mixture is then stirred for 12 hours, the temperature being raised to 23 ° C. Then saturated NaHC0 ₃ solution is added until the gas evolution ceases. The organic phase is separated, extracted with 25 ml of 20% Na ₂ S0 ₃ solution and three times with 25 ml of water. The organic phase is dried with MgS0, filtered and concentrated in vacuo. Yield: 12.1 g.

Example 3: Polymerization Examples:

The following N-oxyl radicals were used:

The tests were carried out in bulk in melted glass tubes. The total mass of each sample was 70 g. Each sample was degassed by bubbling with nitrogen before melting. The melted sample tubes were immersed in aluminum safety containers in a thermostatted oil bath at the desired temperature. The experiments were carried out using styrene as a monomer, benzoyl peroxide as an initiator and in each case an N-oxyl radical. TEMPO (1) and the N-oxyl radical (2) were included for comparison. The following table shows the amounts used, the polymerization time, the conversion achieved, the number average molecular weight (<Mn>) and the polydispersity of the polymer.

* Comparative ^{example χ)} "solid" means a turnover of> 90

Claims

claims

1. N-oxyl radicals of the general formula I,

wherein X is S, NR ⁵ , 0 or SO and

R ¹ and R ² and / or R ³ and R ⁴ together with the carbon atom carrying them represent a ring consisting of at least 3 atoms.

2. N-oxyl radicals according to claim 1, characterized in that R ¹ , R ² , R ³ , R ⁴ and R ⁵ independently of one another for -C-C ₀ alkyl, C ₅ -Cg cycloalkyl, C ₇ -C ₂ o-aralkyl, optionally substituted C ₆ -Cχo-aryl, heteroaryl,

O -R6-OR ⁷ , -R6_o— CH ₂ -CH-0 - R7 ^ _ _R 6 _ ₀ - C - R ⁸ (CH _{2) k} ⁿ

I H

O 0

- R ⁶ -OSiR ⁸ ₃ , - R ⁹ - C— OR ¹⁰ , - R ⁹ - C— NR ⁷ ₂ or -R ⁹ - CN

stand in what

R ⁶ for optionally branched -CC _2u alkylene; R ⁷ each independently for H, -CC _2u alkyl, optionally interrupted by oxygen atoms C ₃ -C ₂₀ cycloalkyl or aryl; R ⁸ each independently Cι-C _υ alkyl or aryl; R ⁹ for a chemical bond or optionally branched Cχ-C o-alkylene; and R ⁱ o is H, C ₁ -C ₂ o-alkyl, aryl or an alkali metal; k for 0 or 1; and n represents an integer from 1 to 100,

or R ¹ and R ² and / or R ³ and R ⁴ together with the C atom carrying them form a carbocyclic ring consisting of 3 to 10 atoms, in which 1 or 2 C atoms are replaced by 0, S or N. and / or in which two non-adjacent atoms can be bridged via a divalent organic radical and / or which can be fused with a further ring.

3. N-oxyl radicals according to claim 2 of the general formula II

wherein X has the meaning given in claim 1,

R ³ and R ⁴ independently of one another for -CC alkyl, phenyl,

Naphthyl or an aromatic five-membered ring or R ³ and R ⁴ together represent - (CH ₂ ) ₀ - and p and o independently of one another represent an integer from 2 to 7.

4. N-oxyl radical generator, characterized in that an N-oxyl radical according to one of claims 1 to 3 is formed as a fragment by homolytic cleavage of a chemical bond.

5. N-oxyl radical generator according to claim 4 of the general formula III,

wherein the symbols X, R ¹ , R ² , R ³ and R ^{4 have} the meaning given in claim 2 and X can additionally stand for S0 ₂ and T stands for an organic radical with a molecular weight of 15 or more. 5

6. The method of free-radically initiated polymerization of ethylenically unsaturated monomers, characterized in that the polymerization in the presence of N-oxyl radicals according to any one of claims 1 to 3, wherein X is additionally for SO ₂

10 can stand, and / or of N-oxyl radical formers according to claim 4 or 5.

7. The method according to claim 6, characterized in that successively different monomers or monomer mixtures po-

15 can be lymerized.

8. The method according to claim 7, characterized in that at least a first monomer in the presence of the N-oxyl radicals and / or N-oxyl radical formers to obtain an intermediate

20 polymerized, the intermediate polymer is optionally isolated and at least one second monomer is polymerized in the presence of the intermediate polymer.

25 9. Use of N-oxyl radicals according to any one of claims 1 to 3 and / or of N-oxyl radical formers according to claim 4 or 5 for the stabilization of ethylenically unsaturated monomers against undesired radical-initiated polymerization.

10. A method for stabilizing compositions containing ethylenically unsaturated monomers against undesired free-radical-initiated polymerization by adding to the composition an effective amount of N-oxyl radicals according to one of claims 1 to 3 and / or of N-oxyl Radikalbild-

35 nern according to claim 4 or 5 there.

11. Use of N-oxyl radicals according to one of claims 1 to 3 and / or of N-oxyl radical formers according to claim 4 or 5 for stabilizing inanimate organic material against light and heat.

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