Classifications

• • C—CHEMISTRY; METALLURGY
  • C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
  • C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
  • C09K21/00—Fireproofing materials
  • C09K21/06—Organic materials
  • C09K21/12—Organic materials containing phosphorus
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
  • C08K9/00—Use of pretreated ingredients
  • C08K9/02—Ingredients treated with inorganic substances

Definitions

• the present invention relates to a process for the preparation of particles containing at least one halogen-free flame retardant and at least one metal or semimetal oxide, wherein the particle is a core-shell particles with flame retardant in the core and metal or semimetal in the shell, or a particle with substantially homogeneous distribution of flame retardant and metal or semimetal oxide, may be.
• the present invention furthermore relates to particles containing at least one halogen-free flame retardant and at least one metal or semimetal oxide, a polymer molding composition containing these particles and at least one thermoplastic or thermosetting polymer, and the use of these particles in polymer molding compositions or for flame retardance of polymer molding and extrusion materials.
• microcapsules having a core-shell structure.
• the shell of these microcapsules is formed by a melamine resin.
• JP 2000263733 discloses a process for impregnating fibrous substrates with phenolic resin paints containing microcapsules containing phosphates.
• Donghua Daxue Xuebao, Ziran Kexue Ban (2007), 33 (6), 701-705 discloses core-shell particles containing water-soluble dimethyl methylphosphonate (DMMP) as a core material and the product of acetalization of PVA and GA (glutaraldehyde) as a shell material , obtainable by an emulsion method.
• DMMP water-soluble dimethyl methylphosphonate
• No particles are known from the prior art which contain a halogen-free, preferably water-insoluble, flame retardant in combination with at least one metal or semimetal oxide, for example SiO 2 , TiO 2 and / or ZnO. Furthermore, no method is disclosed in which, for example, silica is formed by a sol-gel process.
• Object of the present invention over the prior art is thus to bind liquid, halogen-free flame retardants by metal or Halbmetalloxid to convert them into a free-flowing powder.
• the bound liquid, halo Inorganic flame retardants can then be used advantageously in polymer molding compositions.
• step (F) optionally drying the particles from step (E).
• the method 1 according to the invention for producing particles containing at least one halogen-free flame retardant and at least one metal or semimetal oxide comprises at least the following steps
• Step (C) optionally drying the core-shell particles from step (B).
• Step (A): Step (A) of the process 1 according to the invention comprises preparing an aqueous emulsion containing the at least one flame retardant and at least one precursor compound of the at least one metal or semimetal oxide.
• halogen-free flame retardants are used which are preferably insoluble in water.
• halogen-free flame retardants according to the invention are used which, under normal conditions, ie. H. a temperature of 25 ° C and a pressure of about 1 bar (a), are liquid.
• the flame retardants which can be used according to the invention are solid under normal conditions, but melt below 100.degree.
• the flame retardants which can be used according to the invention are generally insoluble in water.
• halogen-free means that the flame retardants which can be used according to the invention do not contain any atoms selected from the halogens, ie fluorine, chlorine, bromine, iodine ..
• no atoms means that the amounts of said atoms below the analytical detection limit.
• Preferred flame retardants according to the present invention are liquid, halogen-free, P-containing flame retardants. These flame retardants are generally known to the person skilled in the art.
• R 1 , R 3 , R 4 , R 5 , R 6 , R 7 , R 8 , R 9 , R 10 , R 11 , R 12 , R 13 , R 14 , R 15 , R 16 , R 17 , R 18 and X independently of one another have the following meanings:
• R 1 , R 3 , R 4 , R 5 , R 6 , R 7 , R 8 , R 9 , R 10 , R 11 , R 12 , R 13 , R 14 , R 15 , R 16 , R 17 , R 18 independently of one another denote hydrogen, hydroxyl group or optionally functional groups bearing aryl, alkyl and / or cycloalkyl radical.
• X is independently oxygen or sulfur.
• An aryl radical according to the invention is a radical having a skeleton of 6 to 30 carbon atoms, preferably 6 to 18 carbon atoms, which is composed of one or more aromatic rings.
• Suitable backbones are, for example, phenyl, naphthyl, anthracenyl or phenanthrenyl. This backbone may be unsubstituted, that is, all carbon atoms which are substitutable bear hydrogen atoms or substituted at one, several or all substitutable positions of the backbone.
• Suitable substituents are for example alkyl groups, preferably atoms alkyl of 1 to 8 carbon, more preferably methyl, ethyl or i-propyl, aryl, preferably C 6 - C 2 2-aryl, more preferably C 6 - C 8 aryl radicals, very more preferably C 6 - C 4 aryl groups, ie aryl groups having a phenyl, naphthyl, phenanthrenyl or anthracenyl backbone which may be substituted or unsubstituted, in turn, heteroaryl, preferably heteroaryl containing at least one nitrogen atom contained ten, more preferably pyridyl groups, alkenyl groups, preferably alkenyl radicals which have a Carrying double bond, more preferably alkenyl radicals having a double bond and 1 to 8 carbon atoms.
• aryl radicals are selected from the group consisting of phenyl, alkyl-substituted phenyl, naphthyl or alkyl-substituted naphthyl.
• an alkyl radical is preferably to be understood as meaning a radical having 1 to 20 carbon atoms, particularly preferably 1 to 10 carbon atoms, very particularly preferably 1 to 8 carbon atoms.
• This alkyl radical may be branched or unbranched and optionally interrupted with one or more heteroatoms, preferably N, O, Si or S.
• this alkyl radical may be substituted by one or more of the substituents mentioned with respect to the aryl groups.
• the alkyl radical carries one or more aryl groups. All of the aryl groups listed above are suitable.
• the alkyl radical (s) to carry one or more functional groups, preferably hydroxyalkyl or cyanoalkyl radicals.
• alkyl radicals are selected from the group consisting of methyl, ethyl, propyl, such as n-propyl, isopropyl, butyl, such as n-butyl, isobutyl, tert-butyl, octyl and its isomers.
• a cycloalkyl radical according to the invention is preferably to be understood as meaning a cyclic radical having 3 to 20 carbon atoms, particularly preferably 3 to 10 carbon atoms, very particularly preferably 3 to 8, for example 3, 4, 5 or 6 carbon atoms.
• This cycloalkyl radical may be substituted or unsubstituted and optionally interrupted by one or more heteroatoms, preferably N, O, Si or S.
• the cycloalkyl radical may be substituted by one or more of the substituents referred to the aryl groups. It is also possible that the cycloalkyl radical carries one or more aryl groups. All of the aryl groups listed above are suitable.
• the cycloalkyl radical (s) to carry one or more functional groups.
• Particularly preferred cycloalkyl radicals are selected from the group consisting of cyclopropyl, cyclobutyl, cyclopentyl, cyclohexyl, and their alkyl-substituted derivatives.
• R 1 to R 18 may carry functional groups.
• Suitable functional groups according to the invention are, for example, selected from the group consisting of carbonyl group, preferably carboxylic acid group, keto group, aldehyde group, ester group, amino group, amide group, hydroxyl group, cyano group, thio group or SCN group.
• R 19 , R 20 , R 21 , R 22 , R 23 , R 24 , R 25 , R 26 , X, Q, L, n and m independently of one another have the following meanings:
• R 19 , R 20 , R 21 , R 22 , R 23 , R 24 , R 25 and R 26 independently of one another are hydrogen or aryl, alkyl and / or cycloalkyl radicals which may carry functional groups.
• X is independently oxygen or sulfur.
• Q and L independently of one another are organic groups which have at least two hydroxyl functions with which the bonds are the P atoms or to a further group Q and L, respectively.
• Q and / or L in the compounds of the general formulas (VII) or (VIII) are independently selected from the group consisting of resorcinol, hydroquinone, bisphenol A, bisphenol F, polycarbonate segments with hydroxy End groups, for example phenolic groups, and mixtures thereof. In these compounds, the hydrogen atoms are split off upon binding to the P. This is known to the person skilled in the art.
• R 19 , R 20 , R 21 and R 22 are preferably phenyl or alkyl-substituted phenyl.
• R 23 , R 24 , R 25 , R 26 are preferably methyl, phenol, phenyl or alkyl-substituted phenyl.
• n is generally independently of one another an integer from 1 to 100, preferably from 1 to 10.
• m is generally independently of one another an integer from 1 to 1000, preferably an integer from 1 to 25.
• the flame retardant additives according to the general formulas (VII) and (VIII) can be present as individual compounds or, preferably, as mixtures of compounds with different values for n and m.
• Compounds of the general formulas (VI) or (VII) which are particularly preferred according to the invention are selected from the group consisting of resorcinol bis (diphenyl phosphate) (formula (VII), R 19 , R 20 , R 21 and R 22 are phenyl, X is oxygen , Q is resorcinol, n is 1 to 7), bisphenol A bis (diphenyl phosphate) (Formula (VII), R 19 , R 20 , R 21 and R 22 are phenyl, X is oxygen, Q is bisphenol A, n is 1 -5), poly (m-phenylenemethyl) phosphonate (formula (VIII), R 23 , R 26 are phenol, R 24 and R 25 are methyl, L is resorcinol,
• At least one metal or semimetal oxide is present in the particles produced. According to the invention, it is possible to use any metal or semi-metal oxide, which is suitable for the production of particles containing at least one flame retardant.
• the at least one metal or hemi-metal oxide is selected from metal or semimetal oxides which can be prepared by the sol-gel process known to the person skilled in the art.
• the at least one metal or semimetal oxide is selected from the group consisting of Si0 2 , Ti0 2 , ZnO, Zr0 2 , Al 2 0 3 and mixtures thereof.
• the precursor compounds of said metal and semimetal oxides are preferably single monomeric units or the precursor compounds are composed of a plurality of monomeric units.
• SiO 2 is used in the process according to the invention.
• the at least one precursor compound of the at least one metal or semimetal oxide is a compound which can be converted into the corresponding metal or semimetal oxide in a sol-gel process known to the person skilled in the art.
• all precursor compounds are suitable which can be converted by the said sol-gel process into the desired metal or semimetal oxide.
• R in which R 27 , R 28 , R 29 and R 30 independently of one another are hydrogen, alkyl, aryl, alkyloxy and / or aryloxy.
• alkyl and / or aryl radicals in the compound of general formula (IX) With respect to the alkyl and / or aryl radicals in the compound of general formula (IX), the above applies.
• the present invention in the compounds of general formula (IX) optionally present alkyloxy and / or aryloxy differ from the said alkyl and / or aryl radicals in that they are attached via an oxygen atom to the Si atom.
• R, R, R and R 30 are particularly preferably selected, independently of one another, from hydrogen, methyl, ethyl, propyl, for example n-propyl, isopropyl, butyl, for example n-butyl, isobutyl, Butyl, tert-butyl, phenyl, methoxy, ethoxy, propoxy, for example, n-propoxy, iso-propoxy, butoxy, for example, n-butoxy, iso-butoxy, tert-butoxy or phenoxy.
• Particularly preferred precursor compounds for SiO 2 are selected from the group consisting of tetraalkoxysilanes, for example tetramethoxysilane (TMOS), tetraethoxysilane (TEOS), methyltrialkoxysilanes, for example methyltrimethoxysilane (MTMS), methyltriethoxysilane (MTES), phenyltrialkoxysilanes, for example phenyltrimethoxysilane (PTMS), phenyltriethoxysilane (PTES ), and mixtures thereof.
• TMOS tetramethoxysilane
• TEOS tetraethoxysilane
• methyltrialkoxysilanes for example methyltrimethoxysilane (MTMS), methyltriethoxysilane (MTES), phenyltrialkoxysilanes, for example phenyltrimethoxysilane (PTMS), phenyltri
• TEOS tetraethoxysilane
• PTES phenyltriethoxysilane
• the quantitative ratio of TEOS to PTES is, for example, 1: 1 to 10: 1, preferably 6: 1 to 3: 1.
• Step (A) of the process 1 of the invention comprises preparing an aqueous emulsion comprising the at least one flame retardant in at least one precursor compound of the at least one metal or semimetal oxide.
• step (A) can generally be carried out by all processes known to those skilled in the art for the preparation of emulsions, for example by combining the individual components in the appropriate amounts.
• the emulsion prepared in step (A) of the process of the invention is aqueous, i. H. the solvent or dispersing agent which is mainly present is water.
• a surfactant particularly a nonionic surfactant, for example selected from the group consisting of alcohol ethoxylates, for example those based on a C 2 alcohol, for example Ci2H 2 5 (OCH 2 CH 2 O) 6 OH, alkylphenol ethoxylates, for example octyl phenol ethoxylates, fatty acid ethoxylates, for example
• Typical nonionic surfactants which are suitable as emulsifier for the emulsion according to the invention are, for example, sorbitan esters and their ethoxylated derivatives. vate, fatty acid esters of sorbitan (so-called spans) and their ethoxylated derivatives (so-called tweens), for example Polyoxyethylensorbitanmonolaurinklareester, Polyoxyethylensorbitanmonooleate, Polyoxyethylensorbitanmonostearate.
• a nonionic surfactant or a mixture of nonionic surfactants is used, its or its concentration is, for example, 0.05 to 5% by weight, preferably 0.5 to 2% by weight, in each case not water-miscible phase, which is formed according to the invention by the at least one non-water-soluble flame retardant.
• the aqueous emulsion according to step (A) may contain at least one non-polar solvent.
• a non-polar solvent is not necessary if a flame retardant is used which dissolves for the most part in the precursor compound of the at least one metal or metalloid oxide.
• Non-polar solvents are generally referred to by those skilled in the art as those solvents having a dielectric constant of less than 15.
• the non-polar solvent which is optionally used in step (A) is a solvent which has a low dielectric constant, for example below 15, and is immiscible with water.
• “Not miscible with water” means that when combined with water permanently form two phases.
• Examples of preferred non-polar solvents used according to the invention are selected from the group consisting of benzene (C 6 H 6 ), carbon tetrachloride (CCI 4 ), diethyl ether (CH 3 CH 2 OCH 2 CH 3 ), pentane, cyclopentane, hexane, cyclohexane, toluene, 1, 4 Dioxane, chloroform, tetrahydrofuran, dichloromethane and mixtures thereof.
• step (A) of the process 1 according to the invention can generally be mixed together in any conceivable order.
• the at least one halogen-free flame retardant is first dissolved or dispersed in a solution of the at least one precursor compound of the at least one metal or semimetal oxide. Preference is then given to the optionally present at least one dissolved non-ionic surfactant in water, and then brought this aqueous solution together with the organic solution.
• step (A) is performed by applying a high shear force to the emulsion so as to achieve efficient mixing of the components.
• the preparation of the emulsion according to step (A) takes place under the action of high shear forces or shear rates.
• the shear rate is preferably 5000 to 10,000 rpm.
• a high-pressure homogenization can be carried out.
• the energy exerted by the high pressure on the emulsion can cause a number of different liquid mechanical effects, such as cavitation, turbulence, shearing, and collisions, which aid in the formation of nanotubes in a homogeneous distribution.
• Step (A) of the process according to the invention can be carried out, for example, by a homogenizing valve or grinding cells, optionally with the action of high pressure, for example 500 to 2000 bar, preferably 800 to 1500 bar.
• a high pressure homogenizer is a microfluidizer.
• the hydrolysis and polycondensation of the sol-gel precursor to the oil-water is preferably carried out in process step B) by setting a suitable pH, for example by acid or base addition Phase boundary initiated.
• Step (B) of the method 1 according to the invention comprises shaping core-shell particles, wherein the at least one flame retardant is present in the core and the at least one metal or semimetal oxide is present in the shell of the particles.
• Step (B) may generally be carried out by any method known to those skilled in the art, by which the precursor compound of the at least one metal or semimetal oxide used in step (A) is converted to the corresponding metal or semimetal oxide.
• the core-shell particles are formed in step (B) by changing the pH in the emulsion.
• the pH can be adjusted by addition of a pH depending on the pH of the starting emulsion Acid or a base can be changed.
• an acid is added in step (B) to provide an emulsion having a pH of from 2 to 6.
• a base is added in step (B) of the process according to the invention to obtain an emulsion having a pH of 8 to 12.
• hydrohalic acids such as hydrochloric acid (HCl), hydrobromic acid (HBr), hydriodic acid (Hl), and their solutions.
• Other suitable acids are halo-oxygen acids, for example hypochlorous acid, chlorous acid, perchloric acid (HCI0 4 ), periodic acid (HI0 4 ).
• sulfuric acid (H 2 S0 4 ) fluorosulfuric acid, nitric acid (HNO 3 ), phosphoric acid (H 3 PO 4 ), fluoroantimonic acid, fluoroboric acid, hexafluorophosphoric acid and chromic acid (H 2 CrO 4 ).
• H 2 S0 4 sulfuric acid
• fluorosulfuric acid fluorosulfuric acid
• HNO 3 nitric acid
• phosphoric acid H 3 PO 4
• fluoroantimonic acid fluoroboric acid
• fluoroboric acid hexafluorophosphoric acid and chromic acid
• chromic acid H 2 Cr
• Preferred bases are, for example, alkali metal hydroxides such as sodium or potassium hydroxide, alkaline earth hydroxides such as calcium hydroxide or ammonia. Particular preference is given to using sodium hydroxide, potassium hydroxide or ammonia. These bases are preferably used in aqueous solution.
• step (B) of process 1 according to the invention the emulsion from step (A) is adjusted to a specific pH with a preferably aqueous solution of at least one of the abovementioned acids or bases.
• This pH is, for example, 2 to 12, preferably 2 to 6 or 8 to 12. Most preferably, a pH of 8 to 10 is set.
• Step (B) may be generally carried out at a temperature of 10 to 80 ° C. Step (B) is carried out in a preferred embodiment for at least two hours, for example 2 to 16 hours.
• the concentration of the at least one liquid halogen-free flame retardant is min. at least 50 wt .-%, particularly preferably at least 60 wt .-%, based on the total weight of the core.
• the core of the particle to be produced according to the invention is a liquid core, very particularly preferably the core is a liquid, oily core.
• the at least one liquid flame retardant present in the core of the core-shell particle to be produced according to the invention is preferably present in the particle in an amount of from 50 to 99% by weight, particularly preferably from 60 to 90% by weight, in each case based on the total particle, in front.
• the at least one metal or semimetal oxide present in the shell of the core-shell particle to be produced according to the invention in the particle is preferably present in an amount of 1 to 50% by weight, particularly preferably 10 to 40% by weight, based in each case on the total Particles, in front.
• the sum of the amounts of at least one flame retardant and at least one metal or semimetal oxide gives 100 wt .-%.
• process steps known to the person skilled in the art such as centrifuging, filtration, evaporation, re-suspension in an aqueous medium or dialysis, may be followed. These optional process steps serve to separate the produced core-shell particles from the liquid components of the emulsion according to the invention.
• the optional step (C) of the process 1 according to the invention comprises the drying of the core-shell particles from step (B).
• the optional step (C) according to the invention is preferably carried out when the core-shell particles obtained from step (B) for the further processing, for example for the production of a polymer molding composition, have too high a proportion of water or other organic solvents , exhibit.
• Step (C) can be carried out according to the invention by all methods known to the person skilled in the art, for example spray-drying.
• the diameter of the particles produced by the process according to the invention 1 particles is, for example, at 0.1 to 100 ⁇ , preferably 0.2 to 20 ⁇ , particularly preferably 0.5 to 5 ⁇ .
• diameter is understood according to the invention the greatest possible distance within the particles produced according to the invention.
• the present invention also relates to a method 2 comprising at least steps (D), (E) and (F). These steps are explained in detail below:
• Step (D) comprises preparing a mixture containing water, at least one polar solvent, at least one halogen-free flame retardant and at least one precursor compound of the at least one metal or semimetal oxide.
• step (D) at least one polar solvent is used.
• polar solvent is understood to be one whose dielectric constant is above 15.
• the at least one polar solvent in step (D) is at least one alcohol.
• Suitable alcohols are selected from the group consisting of methanol, ethanol, propanols such as n-propanol, isopropanol, butanols such as n-butanol, isobutanol, tert-butanol, pentanols such as n-pentanol, isopentanol, tert. Pentanol, methyl pentanol, n-hexanol, dimethyl butanol, ethyl butanol, n-heptanol, n-octyl alcohol, n-nonyl alcohol, n-decyl alcohol, etc.
• the at least one polar solvent is generally present in the mixture in an amount of from 10 to 60% by weight, preferably from 20 to 50% by weight, particularly preferably from 30 to 40% by weight, based in each case on the entire mixture ,
• water is present in the mixture provided in step (D) of process 2 according to the invention.
• Water is generally present in an amount of 5 to 35 wt .-%, preferably 10 to 30 wt .-%, particularly preferably 15 to 25 wt .-%, each based on the total mixture before.
• the at least one halogen-free flame retardant is generally present in the mixture in an amount of from 5 to 40% by weight, preferably from 10 to 30% by weight, particularly preferably from 15 to 25% by weight, based in each case on the entire mixture .
• the at least one precursor compound of the at least one metal or semimetal oxide is generally present in the mixture in an amount of from 10 to 60% by weight, preferably from 20 to 50% by weight, particularly preferably from 30 to 40% by weight, in each case on the whole mix, before.
• the amounts of the components present in the mixture according to step (D) of process 2 according to the invention add up to 100% by weight.
• the mixture prepared in step (D) of process 2 according to the invention may in a preferred embodiment contain a buffer solution.
• a buffer solution is a mixture of a weak acid and its conjugate base or a weak base and its conjugated acid.
• a buffer solution allows that when a small amount of strong acid or base is added, the pH changes only slightly.
• Buffer solutions are used to maintain the pH of a solution at a nearly constant level.
• buffer solutions are aqueous solutions of hydrochloric acid and sodium citrate, citric acid and sodium citrate, acetic acid and sodium acetate, K 2 HP0 4 and KH 2 P0 4 , Na 2 HP0 4 and NaH 2 P0 4 , borax and sodium hydroxide, preferably borax and sodium hydroxide.
• All components present in the mixture according to step (D) of process 2 according to the invention can be mixed together in a manner known to the person skilled in the art, for example with a magnetic stirrer.
• the stirrer speed is generally 100 to 600 rpm, preferably 200 to 500 rpm, more preferably about 300 rpm. It is stirred for a sufficiently long time, for example 2 to 10 minutes.
• Step (E) of the method 2 according to the invention comprises the conversion of the at least one precursor compound of the at least one metal or semimetal oxide into the at least one metal or semimetal oxide in order to obtain a particle which contains at least one metal or Halbmetalloxid and at least one halogen-free flame retardant.
• the conversion of the at least one precursor compound of the at least one metal or semimetal oxide into the at least one metal or semimetal oxide can be carried out in step (E) of the process according to the invention by all methods known to the person skilled in the art.
• step (E) is carried out by heating the mixture of step (D).
• the mixture is heated to a temperature of 30 to 100 ° C, preferably 40 to 80 ° C.
• the heating can be carried out in all reactors known to the person skilled in the art, for example a stir plate hot plate known to the person skilled in the art.
• the heating in step (E) is preferably carried out so that solvent, i. H. Water and / or polar solvent, can escape.
• step (E) preferably forms a gel from the liquid mixture.
• drying may also take place after formation of the gel. This drying is preferably carried out to remove existing solvents, i. H. Separate water and / or polar solvent from the particles. This optional drying also causes aging of the gel to form the particles. The drying is generally carried out at a temperature of 100 to 200 ° C, for example in a spray dryer.
• step (E) By producing a substantially homogeneous mixture in step (D) of the process according to the invention, particles are formed in step (E) in which the at least one halogen-free flame retardant and the at least one metal or semimetal oxide are present in a substantially homogeneous distribution ,
• step (F) of the process according to the invention comprises the drying of the particles from step (E).
• step (F) is carried out.
• the samples from step (E) are each first spray-dried with a mini-spray dryer B-290 (Büchi, Switzerland) to remove the water.
• the spray drying is preferably carried out under the following conditions: inlet temperature of, for example, about 80 to 150 ° C, preferably 1 10 to 130 ° C, z. 120 ° C; Starting temperature of, for example, about 40 to 65 ° C, preferably 45 to 60 ° C, z. B. 55 ° C.
• a two-fluid nozzle is used. Further preferred is the use of nitrogen as a spray gas.
• the particle size of the fine powder obtained in step (F) is, for example, 0.1 to 50 ⁇ m, preferably 0.5 to 20 ⁇ m, particularly preferably 1 to 5 ⁇ m.
• the present invention also relates to particles containing at least one halogen-free flame retardant and a metal or semimetal oxide selected from the group consisting of Si0 2 , Ti0 2 , ZnO, Zr0 2 , Al 2 0 3 , and mixtures thereof.
• the at least one metal or semimetal oxide is Si0 2 .
• the at least one halogen-free flame retardant is particularly preferably selected from the group consisting of triphenylphosphine, diphenyl (o-toluyl) phosphine, tributylphosphine oxide, trioctylphosphine oxide,
• Diphenyl phosphite triphenyl phosphite, tris (nonylphenyl) phosphite,
• Tritoluyl phosphate Tritoluyl phosphate, resorcinol bis (diphenyl phosphate), bisphenol A bis (diphenyl) phosphate, poly (m-phenylene methyl) phosphonate (formula (VIII)) and mixtures thereof.
• the present application also relates to a particle according to the invention wherein it is a core-shell particle in which the at least one halogen-free flame retardant is present in the core and the at least one metal or semimetal oxide in the shell.
• the amount of at least one halogen-free flame retardant in the particle is preferably more than 50% by weight, particularly preferably more than 70% by weight, in each case based on the total particle.
• the ratio between the average thickness of the shell and the mean diameter of the capsule is preferably from 1:20 to 1: 200, more preferably from 1:50 to 1: 100.
• the present invention also relates to a particle according to the invention, wherein the at least one halogen-free flame Protective agent and the at least one metal or Halbmetalloxid are contained in a substantially homogeneous distribution.
• the amount of at least one halogen-free flame retardant in the particle is preferably more than 70% by weight, based in each case on the entire particle.
• the particles produced according to the invention have the advantage that they can be incorporated into a polymeric molding compound more simply from a process engineering point of view than is possible with liquid flame retardants.
• a sticking of the tools used in the production of the molding compound can be avoided.
• a further advantage is that, when using the particles according to the invention in polymeric molding compositions, the undesired softening effect of the flame retardants can be avoided since these are not used in liquid form but in a form bound with a metal or semimetal oxide.
• the flame retardants used in the form according to the invention have a better flame-retarding effect than in the free form.
• the present invention also relates to a leaching out of the flame retardants of polymer molding compositions, which can occur when using liquid flame retardants thermosetting polymer.
• polymers known to the person skilled in the art may be present in the polymer molding composition, for example selected from the group consisting of polyesters such as poly (ethylene terephthalate), poly (butylene terephthalate), poly (trimethylene terephthalate), poly (cyclohexene-dimethylene).
• polyesters such as poly (ethylene terephthalate), poly (butylene terephthalate), poly (trimethylene terephthalate), poly (cyclohexene-dimethylene).
• the particles according to the invention are generally present in an amount of from 1 to 50% by weight, preferably from 1 to 30% by weight, based in each case on the entire polymer molding composition.
• the polymer molding composition of the invention may optionally contain nitrogen-containing synergists such as melamine, melam, Meiern, melamine cyanurate, melamine polyphosphate, Ammonium phosphate, ammonium pyrophosphate, ammonium polyphosphate, and mixtures thereof.
• nitrogen-containing synergists such as melamine, melam, Meiern, melamine cyanurate, melamine polyphosphate, Ammonium phosphate, ammonium pyrophosphate, ammonium polyphosphate, and mixtures thereof.
• nitrogen-containing synergists are preferably present in an amount of 0 to 50 wt .-%, preferably 1 to 50 wt .-%, particularly preferably 1 to 30 wt .-%, each based on the total polymer molding composition, before.
• Antiperspirant reagents and other synergists such as poly (tetrafluoroethylene), zinc oxide, zinc borate, silica, silicates, epoxides and mixtures thereof can optionally be present in the polymer molding composition according to the invention.
• These additives are preferably present in an amount of from 0 to 10% by weight, preferably from 0.2 to 10% by weight, more preferably from 0.2 to 4% by weight, based in each case on the entire polymer molding composition.
• further halogen-free flame retardants may be present in the polymer molding composition according to the invention.
• the amount of these optionally present further halogen-free flame retardants is for example 0 to 30 wt .-%, preferably 0 to 20 wt .-%.
• These flame retardants are, for example, metal phosphinate salts or metal hydroxides.
• polymer additives may be present in the polymer molding composition according to the invention, for example for improving the flameproofing effect, mechanical properties, electrical properties, chemical and hydrolysis properties, etc.
• These polymers include, for example, epoxy polymers, polyacrylates, rubbers, silicones , Maleic anhydride-modified polymers, etc.
• These additives are preferably present in an amount of from 0 to 50% by weight, preferably from 1 to 50% by weight, particularly preferably from 5 to 20% by weight, based in each case on the entire polymer molding composition, in front.
• glass fibers can also be present in the polymer molding composition according to the invention. These glass fibers are preferably present in an amount of 0 to 80 wt .-%, preferably 15 to 30 wt .-%, each based on the total polymer molding composition before.
• Further additives optionally present are selected from the group consisting of slip additives, nucleating agents, stabilizers, crosslinking agents, etc.
• the present invention also relates to a process for preparing the polymer molding composition according to the invention by mixing the particles and the at least one thermoplastic or thermosetting polymer.
• thermoplastic polymers When thermoplastic polymers are used, the mixing can generally be carried out by all methods known to the person skilled in the art, for example by mixing in the melt. Known mixers, kneaders, extruders and blenders can be used, preferably extruders. Single or twin screw extruders of various diameters and volumes may be used. The individual components are preferably mixed together in the molten state. The thermoplastic molding composition obtained can then be converted into a granulate, for example by cutting. From this granules molding parts can be produced according to the invention, for example by injection molding. These methods are known to the person skilled in the art. When using thermoset polymers, for example, epoxy resins or optionally crosslinked, unsaturated polyesters, the components may be reacted together in a standard method involving blending and curing or other known methods. The methods mentioned are known to the person skilled in the art.
• the present invention also relates to the use of a particle according to the invention in polymer molding compositions.
• the present invention also relates to the use of a particle according to the invention for flame retardancy of polymer molding compositions.
• ABS poly (acrylonitrile-butadiene-styrene) containing 38% by weight of styrene
• PTFE poly tetrafluoroethylene
• Ultradur B4300 G6 poly butylene terephthalate resin containing 30% by weight of glass fibers.
• This resin has a viscosity number of 130 ml / g, measured as a 0.5% strength by weight solution in phenol / o-dichlorobenzene, 1 to 1 mixture,
• the silica used is Aerosol 8200.
• Example 1 Encapsulation of RDP in a core-shell structure
• the product is calcined at 280 ° C for 20 minutes in vacuo to remove residual moisture and surfactants.
• the final product is used as compound A in the following examples. After calcination, Compound A contains 7.9 wt% phosphorus, indicating a 73 wt% RDP loading.
• Example 2 Encapsulation of RDP in a core-shell structure 12 g of RDP are dissolved in 9 g TEOS and 3 g PTES solution at room temperature. 0.6 g of Tween 80 are dissolved in 144 g of water. The oil phase is homogenized with the water phase using a high-pressure homogenizer (M-1 10 F microfluidizer, microfluidix) at a pressure of 500 bar for one minute. The finished emulsion is transferred to a 1 L beaker equipped with a magnetic stirrer (300 RPM). 8 g of citric acid-sodium hydroxide-sodium chloride buffer solution (pH 4) are added as a catalyst and the emulsion is stirred for 16 hours.
• M-1 10 F microfluidizer microfluidix
• the suspension is dried by means of a spray dryer, and a fine powder is obtained.
• Example 3 Encapsulation of RDP in a matrix structure
• the product is calcined at 280 ° C for 20 minutes under vacuum to remove residual moisture and surfactant.
• the final product is used as compound B in the following examples. After calcination, Compound B contains 12.9 wt.% Phosphorus, indicating that the loading of PMP is 72 wt.%.
• the FR PC / ABS composition is shown in Table 1.
• the materials are mixed in a 17 mL mini extruder at 280 ° C for three minutes at a screw speed of 80 rpm and are then injection molded into an injection mold under a pressure of 15 bar to produce 1.6 mm diameter UL94 rods , The bars produced are tested according to the UL94 conditions (two consecutive 10 second fires) and were able to extinguish themselves without dripping to meet the V0 requirement.
• the RDP sticks to the feeder and it is difficult to dose.
• the Specimen has a low heat distortion temperature of 85 ° C due to the plasticizer effect of RDP.
• Example 6 Application of encapsulated RDP with a core-shell structure
• Compound A is prepared as described in Example 1.
• the FR PC / ABS composition is shown in Table 1.
• the materials are processed and tested in the same manner as in Example 5.
• Compound A is used in powder form and is easy to dose.
• the rods produced are self-extinguishing without drops and fulfill the VO classification.
• the specimens have a heat deflection temperature of 92 ° C, indicating that the encapsulated RDP can reduce the plasticizer effect of liquid RDP.
• Table 1 Composition and properties of FR PC / ABS
• Example 7 Application of PMP in FR PBT (comparative)
• the FR PBT composition is shown in Table 2.
• the materials are mixed in a 17 ml mini-extruder at a temperature of 260 ° C for three minutes with a screw speed of 80 rpm and then by injection molding in a mold under a pressure of 15 bar in UL 94 bars with 1.6 mm transferred.
• the PMP tends to stick to the feeder and is difficult to dose.
• the filling rate in the mold is 60%.
• the bars produced are tested to UL 94 and burn completely, which corresponds to a UL 94 classification of V-. Due to the plasticizer effect of the PMP, the glass transition temperature of the composite is 27 ° C, significantly lower than standard PBT (40 ° C).
• Example 8 Applications of PMP in FR PBT (Comparison)
• the FR PBT composition with equal loadings of PMP and silica as Example 9 is shown in Table 2.
• the material is processed and tested in the same way as in Example 7. During mixing, the PMP tends to stick to the feeder and is difficult to dose.
• the mold is filled to 50%, less than in Example 7, indicating that the presence of silica increases the melt viscosity of the polymer.
• the bars produced are tested according to UL 94 and are able to extinguish themselves without dripping, which corresponds to the VO classification.
• the glass transition temperature of the composite is 30 ° C.
• Example 9 Applications of encapsulated PMP with a matrix structure
• Compound B is prepared as described in Example 5.
• the FR PBT composition is shown in Table 2.
• the materials are processed and tested in the same way as in Example 7.
• Compound B has a powdery form and is easy to dose.
• the mold is filled to 60%, same as in Example 7, but higher than in Example 8, indicating that the encapsulated PMP does not change the melt viscosity.
• the bars produced are tested to UL 94 and are able to extinguish themselves without dripping, which fulfills the VO classification and which is much better than in Example 7.
• the encapsulated PMP is a better flame retardant than the liquid PMP.
• the glass transition temperature of the composite is 36 ° C, which is higher than in Examples 7 and 8, since the encapsulation of the PMP reduces its softening effects.

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