EP3924425A1 - Verwendung von vinylacetat-copolymeren als low-profile-additiv - Google Patents

Verwendung von vinylacetat-copolymeren als low-profile-additiv

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Publication number
EP3924425A1
EP3924425A1 EP19726335.3A EP19726335A EP3924425A1 EP 3924425 A1 EP3924425 A1 EP 3924425A1 EP 19726335 A EP19726335 A EP 19726335A EP 3924425 A1 EP3924425 A1 EP 3924425A1
Authority
EP
European Patent Office
Prior art keywords
vinyl acetate
isopropenyl
acetate
copolymers
acetate copolymers
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
EP19726335.3A
Other languages
German (de)
English (en)
French (fr)
Inventor
Markus Benjamin BANNWARTH
Michael Tobias Zarka
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Wacker Chemie AG
Original Assignee
Wacker Chemie AG
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Wacker Chemie AG filed Critical Wacker Chemie AG
Publication of EP3924425A1 publication Critical patent/EP3924425A1/de
Pending legal-status Critical Current

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Classifications

    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F218/00—Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by an acyloxy radical of a saturated carboxylic acid, of carbonic acid or of a haloformic acid
    • C08F218/02—Esters of monocarboxylic acids
    • C08F218/04—Vinyl esters
    • C08F218/08—Vinyl acetate
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L67/00—Compositions of polyesters obtained by reactions forming a carboxylic ester link in the main chain; Compositions of derivatives of such polymers
    • C08L67/06—Unsaturated polyesters

Definitions

  • the invention relates to the use of vinyl acetate copolymers as low-profile additives (LPA), free-radically crosslinkable polymer compositions containing the aforementioned low-profile additives and the composite components obtainable therefrom.
  • LPA low-profile additives
  • free-radically crosslinkable polymer compositions based, for example, on unsaturated polyester resins (UP resins) are often used.
  • Unsaturated polyester resins are generally polycondensates of dicarboxylic acids (anhydrides) with polyols.
  • Another component of the free-radically crosslinkable polymer compositions are usually ethylenically unsaturated monomers, such as styrene or methacrylate monomers, in order to dissolve the crosslinkable polymer and to convert the free-radically crosslinkable polymer composition into a flowable mass.
  • peroxides or hydroperoxides can be used as initiators.
  • Radically crosslinkable polymer compositions can also be used, for example, to produce filled solid surfaces or engineered stone products - composite materials made from unsaturated polyester resins or acrylate resins and mineral fillers such as quartz or aluminum trihydrate (ATH).
  • LPAs low-profile additives
  • Low-profile additives reduce shrinkage during curing, relieve residual stresses, reduce microcracking and make it easier to maintain manufacturing tolerances.
  • the low-profile additives also improve the surface quality of the composite components; in particular, Class A surfaces should be achieved, and the imprint of the reinforcement fibers on the component surface should also be prevented (“Fiber print through ").
  • Thermoplastics such as polystyrene, polymethyl methacrylate, saturated polyester or polyvinyl acetate are often used as low-profile additives.
  • Low-profile additives based on polyvinyl acetate and optionally carboxyl-functional monomers are described, for example, in DE-OS 2163089, US Pat. No. 3,718,714 A or in WO 2007/125035 A1.
  • polystyrene and polymethyl methacrylate are characterized by significantly lower shrinkage values and significantly better surface quality of the components, and compared to saturated polyester LPAs by significantly better mechanics.
  • low-profile additives can have a negative effect on the static mechanical properties, such as bending and tensile strengths, of the cured composite component.
  • EP 0031434 recommends low molecular weight epoxidized compounds such as epoxidized plasticizers.
  • VOC volatile organic components
  • FOG fogging; denotes outgassing of condensable substances
  • the object was to provide low-profile additives (LPA) which counteract the volume shrinkage in the course of curing of radically crosslinkable polymer compositions in a more efficient manner. If possible, adequate shrinkage control during curing should be achieved even when using smaller amounts of LPA in polymer compositions which can be crosslinked by free radicals.
  • the LPA should preferably be block-stable. The addition of low molecular weight additives should be avoided if possible.
  • the invention relates to the use of vinyl acetate-isopropenyl acetate copolymers as a low-profile additive (LPA), characterized in that the vinyl acetate-isopropenyl acetate copolymers are based on 2 to 98% by weight of vinyl acetate, 2 to 98% by weight of isopropenyl acetate and optionally one or more further ethylenically unsaturated monomers, each based on the total weight of the vinyl acetate-isopropenyl acetate copolymers.
  • LPA low-profile additive
  • the vinyl acetate-isopropenyl acetate copolymers are based on vinyl acetate to an extent of preferably 50 to 98% by weight, particularly preferably added 65 to 95 weight percent and most preferably 75 to 90 weight percent
  • the vinyl acetate-isopropenyl acetate copolymers are based on preferably 2 to 50% by weight, more preferably 5 to 40% by weight, particularly preferably 8 to 35% by weight, and most preferably 10 to 25% by weight isopropenyl acetate based on the total weight of the vinyl acetate-isopropenyl acetate copolymers.
  • Isopropenyl acetate is also known as 1-methyl vinyl acetate.
  • Vinyl acetate and isopropenyl acetate are vinyl esters of acetic acid.
  • the vinyl acetate-isopropenyl acetate copolymers are preferably based on> 95% by weight, more preferably 3
  • the other ethylenically unsaturated monomers are generally different from vinyl acetate and isopropenyl acetate.
  • ethylenically unsaturated monomers can be, for example, one or more vinyl esters other than vinyl acetate and isopropenyl acetate.
  • vinyl esters are vinyl propionate, vinyl butyrate, vinyl 2-ethylhexanoate, vinyl laurate, vinyl pivalate and vinyl esters of alpha-branched monocarboxylic acids having 5 to 13 carbon atoms, for example VeoVa9R, VeoValOR or VeoVallR (trade names from Shell).
  • the vinyl acetate-isopropenyl acetate copolymers are based preferably ⁇ 5% by weight, more preferably £ 3% by weight and particularly preferably £ 1% by weight on vinyl esters other than vinyl acetate and isopropenyl acetate, based on the total weight of the vinyl acetate-isopropenyl acetate. Copolymers. Most preferred are vinyl acetate-isopropenyl acetate copoly- mers that do not contain units of vinyl esters other than vinyl acetate and isopropenyl acetate.
  • Preferred further ethylenically unsaturated monomers are ethylenically unsaturated acids or their salts, in particular carboxylic acids such as acrylic acid, methacrylic acid, crotonic acid, itaconic acid and fumaric acid, maleic acid, monoesters of fumaric acid or maleic acid or their salts, such as the ethyl and isopropyl esters; ethylenically unsaturated sulfonic acids or their salts, preferably vinylsulfonic acid, 2-acrylamido-2-methyl-propanesulfonic acid; ethylenically unsaturated phosphonic acids or their salts, preferably vinylphosphonic acid.
  • carboxylic acids such as acrylic acid, methacrylic acid, crotonic acid, itaconic acid and fumaric acid
  • maleic acid monoesters of fumaric acid or maleic acid or their salts, such as the ethyl and isopropyl esters
  • Ethylenically unsaturated carboxylic acids or their salts are particularly preferred. Acrylic acid, methacrylic acid and crotonic acid are most preferred.
  • the vinyl acetate-isopropenyl acetate copolymers are based on ethylenically unsaturated acids or their salts in an amount of preferably 0 to 5% by weight, particularly preferably 0.1 to 3% by weight and most preferably 0.5 to 2% by weight based on the total weight of the vinyl acetate-isopropenyl acetate copolymers.
  • ethylenically unsaturated monomers are one or more monomers selected from the group comprising methacrylic esters or acrylic esters of carboxylic acids with unbranched or branched alcohols having 1 to 15 carbon atoms, vinyl aromatics, vinyl halides, dienes and olefins.
  • Such monomers are preferably ⁇ 5% by weight, more preferably £ 3% by weight and particularly preferably £ 1% by weight polymerized into the vinyl acetate-isopropenyl acetate copolymers, based on the total weight of the vinyl acetate-isopropenyl acetate copolymers. Most preferably, no such monomers are polymerized into the vinyl acetate-isopropenyl acetate copolymers.
  • the vinyl acetate-isopropenyl acetate copolymers have glass transition temperatures Tg of preferably 20 to 70 ° C, particularly preferably 30 to 50 ° C and most preferably 35 to 45 ° C.
  • the selection of monomers or the selection of the proportions by weight of the individual monomers is preferably carried out in such a way that the above-mentioned glass transition temperatures Tg of the vinyl acetate isopro- penyl acetate copolymers are obtained.
  • the glass transition temperature Tg can be determined in a known manner by means of differential scanning calorimetry (DSC).
  • the Tg can also be approximately calculated in advance using the Fox equation. According to Fox T. G., Bull. Am. Physics Soc.
  • the vinyl acetate-isopropenyl acetate copolymers have molecular weights Mw of preferably 2,000 to 750,000 g / mol, particularly preferably from 20,000 to 300,000 g / mol and most preferably from 50,000 to 200,000 g / mol (method of determination: SEC ("Size Exclusion Chromatography") below Use of a polystyrene standard in THF at 60 ° C).
  • the vinyl acetate-isopropenyl acetate copolymers have a Höppler viscosity of preferably 1 to 100 mPas, particularly preferably 2 to 20 mPas, even more preferably 3 to 10 mPas and most preferably 5 to 9 mPas (Höppler method at 20 ° C., DIN 53015, in 10% solution in ethyl acetate).
  • the vinyl acetate-isopropenyl acetate copolymers are preferably not emulsifier-stabilized and / or preferably not
  • the vinyl acetate-isopropenyl acetate copolymers are generally obtainable by means of polymerization of the ethylenically unsaturated monomers according to the invention in the presence of free radical initiators, in particular by means of radical initiated substance, solution or suspension polymerization processes.
  • the solution polymerization method is particularly preferred.
  • the solvent used is preferably an organic solvent or a mixture of organic solvents or a mixture of one or more organic solvents and water.
  • Preferred solution mediums are alcohols, ketones, esters, ethers, aliphatic hydrocarbons, aromatic hydrocarbons and water.
  • Particularly preferred solvents are aliphatic alcohols with 1 to 6 carbon atoms, such as methanol, ethanol, n-propanol or i-propanol, ketones such as acetone or methyl ethyl ketone, esters such as methyl acetate, ethyl acetate, propyl acetate or butyl acetate, or water. Most preferred are methanol, i-propanol, methyl acetate, ethyl acetate and butyl acetate.
  • the temperature during the polymerization is preferably from 20 ° C. to 160 ° C., particularly preferably from 40 ° C. to 140 ° C.
  • the polymerization is carried out at normal pressure, preferably under reflux.
  • Suitable free radical initiators are, for example, oil-soluble
  • Initiators such as t-butyl peroxy-2-ethylhexanoate, t-butyl peroxy pivalate, t-butyl peroxyneodecanoate, dibenzoyl peroxide, t-amyl peroxypivalate, di- (2-ethylhexyl) peroxydicarbonate, 1,1-bis (t-butyl peroxy) -3,3,5-trimethylcyclohexane and di- (4-t-butylcyclohexyl) peroxydicarbonate.
  • azo initiators such as
  • the initiators are generally used in an amount of 0.005 to 3.0% by weight, preferably 0.01 to 1.5% by weight, based in each case on the total weight of the monomers for the preparation of the vinyl acetate-isopropenyl acetate copolymers. set.
  • the rate of polymerization can be controlled, for example, by the temperature, the initiators, by using initiator accelerators or by the initiator concentration.
  • the setting of the molecular weight and the degree of polymerization is known to the person skilled in the art. This can be done, for example, by adding regulators, by the ratio of solvent to monomers, by varying the initiator concentration, by varying the dosage of monomers and by varying the polymerization temperature.
  • Regulators or chain transfer agents are, for example, alcohols such as methanol, ethanol and isopropyl alcohol nol, aldehydes or ketones, such as acetaldehyde, propionaldehyde, butyraldehyde, acetone or methyl ethyl ketone, but also compounds containing mercapto groups, such as dodecyl mercaptan, mercapto propionic acid or silicones containing mercapto groups.
  • alcohols such as methanol, ethanol and isopropyl alcohol nol
  • aldehydes or ketones such as acetaldehyde, propionaldehyde, butyraldehyde, acetone or methyl ethyl ketone
  • compounds containing mercapto groups such as dodecyl mercaptan, mercapto propionic acid or silicones containing mercapto groups.
  • the polymerization can be carried out with the introduction of all or individual constituents of the reaction mixture, or with partial introduction and subsequent metering of all or individual constituents of the reaction mixture, or according to the metering process without introduction.
  • Volatile residual monomers or other volatile constituents can be removed, for example, by means of distillation or stripping processes, preferably under reduced pressure.
  • the invention furthermore relates to polymer compositions containing free-radically crosslinkable
  • At least one initiator in particular peroxides or hydroperoxides
  • accelerators such as cobalt or amine-based accelerators
  • the vinyl acetate-isopropenyl acetate copolymers function as LPA in the free-radically crosslinkable polymer compositions.
  • the free-radically crosslinkable polymer compositions contain the vinyl acetate-isopropenyl acetate copolymers in an amount of preferably 2 to 20% by weight and particularly preferably 4 to 16% by weight, based on the total weight of resin a) and monomer b) and vinyl acetate-isopropenyl acetate copolymer.
  • the vinyl acetate-isopropenyl acetate copolymers are in the form of a 10 to 70% by weight solution, preferably 30 to 55% by weight solution, in ethylenically unsaturated monomers, preferably styrene or methacrylates, such as methyl methacrylate (MMA), 1,3-butanediol dimethacrylate (1,3-BDMA) and 1,4-butanediol dimethacrylate (1,4-BDDMA) are used.
  • MMA methyl methacrylate
  • 1,3-butanediol dimethacrylate (1,3-BDMA) and 1,4-butanediol dimethacrylate (1,4-BDDMA) are used.
  • the vinyl acetate-isopropenyl acetate copolymers are particularly preferably used in a 35 to 55% strength by weight solution in styrene, 1,4-BDDMA or 1,3-BDDMA.
  • Components a) to g) and their amounts used in the free-radically crosslinkable polymer compositions can in principle be selected in a conventional manner by the person skilled in the art in accordance with the requirements of the particular application.
  • Unsaturated polyester resins suitable as resin a) are generally accessible by polycondensation of unsaturated and saturated dicarboxylic acids or dicarboxylic acid anhydrides with polyols.
  • Vinyl ester resins VE resins suitable as resin a) are obtainable, for example, by esterifying epoxy resins with acrylic or methacrylic acid. Suitable UP resins and VE resins are also available commercially.
  • the free-radically crosslinkable polymer compositions also contain monomers b) with ethylenically unsaturated groups, generally styrene or methacrylate monomers such as methyl methacrylate (MMA) or 1,3- and 1,4-butanediol dimethacrylate (1,3-BDDMA / 1,4-BDDMA) .
  • monomers b) with ethylenically unsaturated groups generally styrene or methacrylate monomers such as methyl methacrylate (MMA) or 1,3- and 1,4-butanediol dimethacrylate (1,3-BDDMA / 1,4-BDDMA) .
  • MMA methyl methacrylate
  • 1,4-butanediol dimethacrylate 1,3-BDDMA / 1,4-BDDMA
  • the addition of the initiators c) to the free-radically crosslinkable polymer compositions generally serves to initiate the crosslinking of the unsaturated polyester or vinyl ester resin.
  • Common peroxides or hydroperoxides can be used in common amounts, for example cumene hydroperoxide, dibenzoyl peroxide or methyl ethyl ketone peroxide.
  • the free-radically crosslinkable polymer compositions optionally also contain accelerators d).
  • Accelerators d) can serve to accelerate the decomposition of the initiator.
  • Suitable accelerators and the amounts used are generally known to the person skilled in the art and are commercially available, for example, such as cobalt salts, in particular cobalt octoate, cobalt neodecanoate or cobalt naphtenate.
  • Preferred free-radically crosslinkable polymer compositions contain no accelerators d).
  • the free-radically crosslinkable polymer compositions can optionally contain fiber materials e) or fillers f) or additives such as processing aids, in particular thickeners.
  • the invention also provides composite components obtainable by curing the radically crosslinkable polymer compositions according to the invention.
  • the curing of the free-radically crosslinkable polymer compositions is preferably carried out at temperatures of 3 40 ° C, particularly preferably from 60 ° C to 180 ° C and most preferably from 70 to 130 ° C. Curing is preferably carried out in the presence of one or more initiators by free-radically initiated polymerization.
  • the free-radically crosslinkable polymer compositions are optionally pressed during curing at the respective temperature using pressures of 3 1 mbar, particularly preferably from 1 to 200,000 mbar and most preferably from 1,000 to 200,000 mbar.
  • the composite components can be obtained from the radically crosslinkable polymer compositions by all common manufacturing processes, preferably by means of Sheet Molding Compound Technology (SMC), Bulk Molding Compound Technology (BMC), Resin Transfer Molding (RTM), pultrusion, continuous lamination or resin injection Molding (RIM).
  • SMC Sheet Molding Compound Technology
  • BMC Bulk Molding Compound Technology
  • RTM Resin Transfer Molding
  • pultrusion continuous lamination
  • continuous lamination resin injection Molding
  • RIM resin injection Molding
  • the isopropenyl acetate-vinyl acetate copolymers according to the invention when used as LPA in free-radically crosslinkable polymer compositions, show a surprisingly strong shrinkage-reducing effect in the course of their curing. This applies even if only relatively small amounts of isopropenyl acetate-vinyl acetate copolymers are added to the free-radically crosslinkable polymer compositions.
  • the LPAs according to the invention are also surprisingly block-stable, even without the addition of antiblocking agents such as carbonates, talc, gypsum, silica, kaolins or silicates.
  • the LPA according to the invention can advantageously also be granulated and provided in the form of block-stable granules. All these effects were all the more surprising since isopropenyl acetate is structurally similar to vinyl acetate and yet the proportion of isopropenyl acetate units according to the invention in the LPA according to the invention considerably increased their LPA efficiency.
  • the following examples serve to further explain the invention without restricting it in any way. Production of vinyl acetate-isopropenyl acetate copolymers:
  • the Höppler viscosity of the copolymer determined according to DIN 53015 (10% in ethyl acetate at 20 ° C.), 7.2 mPas, its number-average molecular weight M n was 24,700 g / mol, its weight-average molecular weight M w was 114,300 g / mol, determined by size exclusion chromatography in THF at 60 ° C against narrowly distributed polystyrene standards.
  • the glass transition temperature Tg of the copolymers was 38.7 ° C.
  • Example 2 Example 2:
  • VAc-IPAc copolymer with 15% IPAc (LPA2):
  • the Höppler viscosity of the copolymer determined according to DIN 53015 (10% in ethyl acetate at 20 ° C.), 8.7 mPas, its number average molecular weight M n was 34,000 g / mol, its weight average molecular weight M w was 143,100 g / mol, determined by size exclusion chromatography in THF at 60 ° C against narrowly distributed polystyrene standards.
  • the glass transition temperature Tg of the copolymers (determined by means of differential scanning calorimetry (DSC)) was 41.3 ° C.
  • VAc-IPAc copolymer with 30% IPAc (LPA3):
  • the Höppler viscosity of the copolymer determined according to DIN 53015 (10% in ethyl acetate at 20 ° C.), 6.3 mPas, its number average molecular weight M n was 35,600 g / mol, its weight average molecular weight M w was 117,100 g / mol, determined by size exclusion chromatography in THF at 60 ° C against narrowly distributed polystyrene standards.
  • the glass transition temperature Tg of the copolymers (determined by means of differential scanning calorimetry (DSC)) was 42.9 ° C.
  • DSC differential scanning calorimetry
  • the Höppler viscosity of the copolymer determined according to DIN 53015 (10% in ethyl acetate at 20 ° C.), 4.9 mPas, its number average molecular weight M n was 26,000 g / mol, its weight average molecular weight M w was 96,800 g / mol, determined by size exclusion chromatography in THF at 60 ° C against narrowly distributed polystyrene standards.
  • the glass transition temperature Tg of the copolymers was 46.0 ° C.
  • a mixture was produced from the raw materials listed in Table 1 and briefly degassed.
  • the density Dv of the degassed mixture was determined, then the mixture was poured into a mold, cured at 120 ° C. for 2 hours and then post-cured for 24 hours at room temperature. Finally, the density D H of the cured molding was determined.
  • the density was determined using the DMA 38 density meter (trade name of Anton Paar) at 23 ° C.
  • LPA low-profile additives
  • LPA1 Example 1 (5% IPAc);
  • LPA4 Example 3 (30% IPAc, 1% crotonic acid);
  • VAc-IPAc copolymers LPAl, LPA2 and LPA3 according to the invention show a significant reduction in shrinkage at the same dosage, the LPA effect increasing with increasing IPAc content in the copolymer and even slight expansion being observed from 30% IPAc.
  • the VAC-IPAc-crotonic acid terpolymer LPA4 according to the invention with 30% IPAc and 1% crotonic acid also shows excellent shrinkage compensation to 0.4%.
  • Table 2 Shrinkage of the moldings:
  • a mixture was produced from the raw materials listed in Table 3 and briefly degassed.
  • the density Dv of the degassed mixture was determined, then the mixture was poured into a mold, hardened at 120 ° C. for 2 hours and then post-hardened at room temperature for 24 hours. Finally, the density DH of the cured molded body was determined.
  • the density was determined using the DMA 38 density meter (trade name of Anton Paar) at 23 ° C.
  • Table 4 shows that the conventional LPA (LPAV1) is effective with a medium LPA content, but the VAc-1PAc copolymers LPA1, LPA2 and LPA3 according to the invention show a significantly improved reduction in shrinkage or even a significant expansion. With an increasing IPAc content in the copolymer, the shrinkage decreases significantly and the volume increase increases significantly.
  • a mixture was produced from the raw materials listed in Table 3 and briefly degassed.
  • the density Dv of the degassed mixture was determined, then the mixture was poured into a mold, cured at 80 ° C. for 2 hours and then post-cured at room temperature for 24 hours. Finally, the density DH of the cured molded body was determined.
  • the density was determined using the DMA 38 density meter (trade name of Anton Paar) at 23 ° C.
  • Table 5 shows that the conventional LPA LPAV1 is effective at a medium LPA content, but the invention
  • VAc-IPAc copolymers LPA1, LPA2 and LPA3 show a significantly improved reduction in shrinkage.
  • the LPA effect improves.
  • the UP resin and all additives (see Table 6) except for the glass fibers and the filler (calcium carbonate) were premixed for 2 minutes in a container with a dissolver (resin paste).
  • this resin paste was premixed with the glass fibers and calcium carbonate for 15 minutes in a small laboratory kneader.
  • the BMC compound (Bulk Molding Compound) was then packed in styrene-tight with suitable foils and stored for 2 days at 23 ° C (maturing time) and then placed in a Wickert press (pressing conditions: 3 minutes, 160 ° C, 730 kN pressing force, 3 mm board thickness).
  • the BMC plates obtained in this way were tested as follows after cooling to room temperature:
  • BMC 2 with the LPA4 according to the invention shows a better surface quality compared with BMC 1 with the Vinnapas® C 501 not according to the invention, which is shown in a higher gloss and in lower long wave and short wave values.
  • the linear shrinkage is also lower with BMC 2.
  • the flexural modulus of elasticity - a measure of the rigidity of the composite component - is somewhat improved in the BMC 2 according to the invention.

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  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Compositions Of Macromolecular Compounds (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
EP19726335.3A 2019-05-15 2019-05-15 Verwendung von vinylacetat-copolymeren als low-profile-additiv Pending EP3924425A1 (de)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
PCT/EP2019/062531 WO2020228953A1 (de) 2019-05-15 2019-05-15 Verwendung von vinylacetat-copolymeren als low-profile-additiv

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EP3924425A1 true EP3924425A1 (de) 2021-12-22

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Country Status (4)

Country Link
US (1) US20220259344A1 (zh)
EP (1) EP3924425A1 (zh)
CN (1) CN113631658B (zh)
WO (1) WO2020228953A1 (zh)

Family Cites Families (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5231911B1 (zh) * 1970-02-02 1977-08-18
US3718714A (en) 1970-09-16 1973-02-27 Union Carbide Corp Unsaturated polyester compositions
DE2163089B2 (de) 1971-12-18 1977-09-08 Chemische Werke Hüls AG, 4370 Mari Ungesaettigte polyesterformmasse
CA1171585A (en) 1979-11-13 1984-07-24 Kenneth E. Atkins Composition containing an unsaturated polyester, a low profile thermoplastic polymer additive, a polymerizable monomer and an epoxy compound
US4555534A (en) * 1981-03-26 1985-11-26 Union Carbide Corporation Uniformly pigmented, low shrinking polyester molding compositions
DE4030638A1 (de) * 1990-09-27 1992-04-02 Wacker Chemie Gmbh Dispersionspulverzusammensetzung
DE10040171A1 (de) * 2000-08-17 2002-03-07 Wacker Chemie Gmbh Verwendung von acetalisierten Vinylalkoholpolymerisaten als Verdickungsmittel
DE10040178A1 (de) * 2000-08-17 2002-03-07 Wacker Chemie Gmbh Verdickungsmittel auf der Basis von Vinylalkohol-Mischpolymerisaten
DE102006019686A1 (de) 2006-04-27 2007-10-31 Wacker Polymer Systems Gmbh & Co. Kg Verwendung von carboxylfunktionellen Polyvinylacetaten zur Herstellung von BMC-Formteilen

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US20220259344A1 (en) 2022-08-18
CN113631658A (zh) 2021-11-09
CN113631658B (zh) 2023-04-28
WO2020228953A1 (de) 2020-11-19

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