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Low-emission dispersion paints, coating materials and synthetic resin dispersion plasters as well as processes for the preparation thereof    

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United States Patent5576384   
Link to this pagehttp://www.wikipatents.com/5576384.html
Inventor(s)N olken; Ernst (Bad Soden am Taunus, DE); Braun; Helmut (Kriftel, DE); Lonitz; Michael (Trechtingshausen, DE)
AbstractProduction of low-emission dispersion paints, coating materials and synthetic resin dispersion plasters in the form of aqueous preparations based on aqueous synthetic resin dispersion copolymers derived from olefinically unsaturated monomers, having a pigment volume concentration (PVC) of at least 60% and containing water, fillers, pigments, synthetic resin dispersion copolymers and conventional auxiliaries, wherein the synthetic resin dispersion copolymers have a content of 0.05 to 2% by weight of monomer units derived from special unsaturated hydrolyzable organic silicon compounds and the aqueous copolymer dispersions possess a minimum film-forming temperature (MFT) of <10.degree. C., preferably <5.degree. C. and especially <2.degree. C., the aqueous preparations according to the invention contain <0.1% by weight of volatile non-aqueous constituents, based on the total non-volatile part of the preparations, and the pH of the aqueous preparations is in the range from 5.5 to 10.
   














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Inventor     N olken; Ernst (Bad Soden am Taunus, DE); Braun; Helmut (Kriftel, DE); Lonitz; Michael (Trechtingshausen, DE)
Owner/Assignee     Hoechst AG (DE)
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Publication Date     November 19, 1996
Application Number     08/447,389
PAIR File History     Application Data   Transaction History
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Litigation
Filing Date     May 23, 1995
US Classification     524/806 524/457
Int'l Classification     C08L 083/04
Examiner     Smith; Jeffrey T.
Assistant Examiner    
Attorney/Law Firm     Bierman and Muserlian
Address
Parent Case     PRIOR APPLICATIONS This application is a continuation of U.S. patent application Ser. No. 855,734 filed Mar. 19, 1992 which is a continuation of U.S. patent application Ser. No. 633,276 filed Dec. 24, 1990 which is a continuation of U.S. patent application Ser. No. 306,881 filed Feb. 3, 1989, all now abandoned.
Priority Data     Feb 05, 1988[DE]38 03 450.6
USPTO Field of Search     524/457 524/806 524/837
Patent Tags     low-emission dispersion paints, coating materials synthetic resin dispersion plasters well preparation
   
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We claim:

1. A low emission dispersion paint, coating material and synthetic resin dispersion plaster in the form of aqueous preparations based on aqueous synthetic resin dispersion polymers derived from olefinically unsaturated monomers having a pigment volume concentration (PVC) of at least 60% and containing water, fillers, pigments, synthetic resin dispersion polymers and auxiliaries selected from the group of wetting agents, disperants, emulsifiers, protective colloids, thickeners, antifoams, dyes and preservatives, wherein the non-volatile part of the aqueous preparations contains

35 to 94% by weight of a filler,

2 to 30% by weight of pigment,

0.1 to 10% by weight of an auxiliary and

4 to 35% by weight of synthetic resin dispersion

copolymer, based on the total non-volatile part, the aqueous dispersion of which copolymer possesses a minimum film-forming temperature (MFT) of <10.degree. C., and the synthetic dispersion copolymer has a content of 0.05 to 0.4% by weight of monomeric units derived from unsaturated hydrolyzable organic silicon compounds of the formula ##STR3## in which R denotes an organic radical olefinically unsaturated in the .sup..omega. -position and R.sup.1, R.sup.2 and R.sup.3 which may be identical or different, denote halogen or the group -OZ, Z denoting primary or secondary alkyl radicals or acyl radicals optionally substituted by alkoxy groups, or hydrogen, the content of volatile non-aqueous constituents of the aqueous preparations being 0.1% by weight, based on the total non-volatile part, and the pH of the aqueous preparation being in the range from 5.5 to 10 wherein after the copolymer having been copolymerized, residual monomers being removed by distillation.

2. A paint as claimed in claim 1 wherein the synthetic resin dispersion copolymer contains monomeric units selected from the group consisting of vinyl esters, vinyl esters/ethylene, vinyl esters/vinyl chloride/ethylene, vinyl esters/vinyl versatates, vinyl esters/acrylic esters and acrylic esters/vinyl versatates/ethylene.

3. A paint as claimed in claim 1 wherein the synthetic resin dispersion copolymer compounds are selected from the group consisting of .gamma.-acryloxy-propyltrimethoxysilane, .gamma.-methacryloxypropyltrimethoxysilane, vinyltrimethoxysilane, vinyltriethoxysilane, vinyltrimethylgycol-silane, vinyltriacetoxysilane, vinyltrichlorosilane, vinylmethyl-dichlorosilane and .gamma.-methacryloxypropyltris(2-methoxy-ethoxy) silane as hydrolyzable monomeric units of the formula I.

4. A paint as claimed in claim 1 wherein the synthetic resin dispersion copolymer comprises mixtures of dispersion copolymers, a part of which contains no monomeric units of the formula I and another part of which contains monomeric units of formula I in such an amount that the mean content of monomeric units of formula I in the total dispersion copolymer mixture is 0.05 to 2% by weight, based on the total synthetic resin dispersion copolymer mixture.

5. A paint as claimed in claim 1 wherein the mean particle diameter of the synthetic resin dispersion copolymer particles is at least in the neighborhood of 0.1 .mu.m or higher.

6. A paint as claimed in claim 1 wherein the aqueous preparations are free from residual monomers, from lower alcohols and from ammonia and/or volatile amines or from components which give rise by cleavage to H.sub.2 S or mercaptans, if appropriate, and the total content of volatile non-aqueous constituents of the aqueous preparations is <0.05% by weight, based on the total non-volatile part.

7. A paint as claimed in claim 1 wherein the synthetic resin dispersion copolymer contained in the aqueous preparations and carrying silicon radicals from monomeric units of the formula I was prepared by radically initiated copolymerization of the finely divided monomers having an amount of 0.05% to 2% by weight, based on the total amount of monomer, of monomers of the formula I in aqueous medium with the simultaneous use of hydroxyethylcellulose, nonionic emulsifiers and monomeric sodium vinylsulfonate as emulsifier/protective colloid system, and the volatile alcohol components which may have formed by hydrolysis from the monomeric units of the formula I in the aqueous dispersion and any volatile amounts of residual monomers which may be present after the terminated polymerization reaction have been removed by distillation under reduced pressure.

8. A paint of claim 1 wherein the synthetic resin dispersion copolymer has a content of 0.1 to 0.4% by weight of monomeric units derived from unsaturated hydrolyzable organic silicon compounds of formula I.

9. A low emission dispersion paint, coating material and synthetic resin dispersion plaster in the form of aqueous preparations based on aqueous synthetic resin dispersion polymers derived from olefinically unsaturated monomers having a pigment volume concentration (PVC) of at least 60% and containing water, fillers, pigments, synthetic resin dispersion polymers and auxiliaries selected from the group of wetting agents, disperants, emulsifiers, protective colloids, thickeners, antifoams, dyes and preservatives, wherein the non-volatile part of the aqueous preparations contains

35 to 94% by weight of a filler,

2 to 30% by weight of pigment,

0.1 to 10% by weight of an auxiliary and

4 to 35% by weight of synthetic resin dispersion

copolymer, based on the total non-volatile part, the aqueous dispersion of which copolymer possesses a minimum film-forming temperature (MFT) of <10.degree. C., and the synthetic dispersion copolymer has a content of 0.05 to 0.4% by weight of monomeric units derived from unsaturated hydrolyzable organic silicon compounds of the formula ##STR4## in which R denotes an organic radical olefinically unsaturated in the .sup..omega. -position and R.sup.1, R.sup.2 and R3 are individually -OZ, Z being primary or secondary alkyl, the content of volatile non-aqueous constituents of the aqueous preparations being <0.1% by weight, based on the total non-volatile part, and the pH of the aqueous preparations being in the range from 5.5 to 10 wherein after the copolymer having been copolymerized, volatile alcohol components formed by hydrolysis from the monomeric units of formula I and volatile amounts of residual monomers being removed by distillation.
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The invention relates to low-emission dispersion paints, coating materials and synthetic resin dispersion plasters in the form of aqueous preparations based on aqueous synthetic resin dispersions having a pigment volume concentration (PVC) of at least 60% which are free from organic solvents and volatile organic film-forming auxiliaries and low-molecular weight plasticizers, and which are free from readily volatile non-aqueous constituents and from malodorous by-products, furthermore to processes for the preparation thereof and to the use thereof as construction protective materials and as structural materials, especially in spaces that are inadequately ventilated and are inhabitated.

In order to reduce pollution by noxious substances it is often desirable for aqueous dispersion paints, coating materials and synthetic resin dispersion plasters, when used in the open or especially in enclosed spaces, to be unable to liberate, apart from water, any non-aqueous volatile organic or inorganic constituents.

However, according to the state of the art, construction protective materials such as, for example dispersion paints, plasters, mastics, and liquid adhesives, contain more or less large amounts of solvents. The readily volatile or the moderately to slightly volatile additives here used as solvents or film-consolidating or film-forming auxiliaries or also as plasticizers, are generally indispensable for achieving the required application properties of the construction protective materials. In order to attain high wet abrasion resistance, mechanical strength, low tendency to soiling and to blocking of the used materials, it has not been hitherto possible to employ dispersion polymers whose aqueous dispersions possess a freezing or glass temperature (Tg) or a minimum film-forming temperature (MFT) in the neighborhood of 0.degree. C. These application properties could accordingly only be achieved by the use of polymer dispersions having a Tg or MFT distinctly above 0.degree. C. in conjunction with film-forming auxiliaries which reduce the Tg or MFT, with the result that it was possible to employ them even at, or, if desired, below 5.degree. C. Film-forming auxiliaries and temporary-plasticizers, however, migrate into the atmosphere on drying, which may be toxicologically hazardous especially with indoor paints, for example through unpleasant odor or through inhalation by sensitive persons.

Permanent plasticizers have also been used in the past. This can lead to shortcomings due to increased tackiness, plasticizer migration as well as to possible volatility.

Experiments were also undertaken into using vinyl acetate dispersion copolymers, especially vinyl acetate/ethylene copolymer dispersions which possess a Tg or a MFT in the neighborhood of 0.degree. C.

It was found, however, that the pigment binding power of such dispersions is limited compared with systems having binders obtained from harder dispersion copolymers with additions of film-consolidating auxiliaries.

Thus the object forming the basis of the present invention has been to make available such aqueous dispersion paints, coating materials and plasters which contain no significant proportions of non-aqueous volatile compounds apart from water and which contain as binders synthetic resin dispersions which are free from film-forming auxiliaries, and which have a high pigment binding power per se and moreover whose films possess low tendency to soiling and to blocking even at a low Tg or low MFT of the dispersion.

It has now been found, surprisingly, that the foregoing difficulties may be overcome by using dispersions of such synthetic resin dispersion copolymers whose copolymer macromolecules contain small amounts of monomeric units derived from unsaturated hydrolyzable organic silicon compounds and possess the required Tg and MFT values, and furthermore the dispersions are virtually free from volatile non-aqueous organic and/or inorganic constituents.

Accordingly, the subject matter of the invention are low-emission dispersion paints, coating materials and synthetic resin dispersion plasters in the form of aqueous preparations based on aqueous synthetic resin dispersion polymers derived from olefinically unsaturated monomers having a pigment volume concentration (PVC) of at least 60% and containing water, fillers, pigments, synthetic resin dispersion polymers and auxiliaries selected from the group wetting agents, dispersants, emulsifiers, protective colloids, thickeners, antifoams, dyes and preservatives, wherein the non-volatile part of the aqueous preparations contains

35 to 94% by weight of a filler,

2 to 30% by Weight of a pigment,

0.1 to 10% by weight of an auxiliary and

4 to 35% by weight of a synthetic resin dispersion copolymer, based on the total non-volatile part, the aqueous dispersion of which copolymer possesses a minimum film-forming temperature (MFT) of <10.degree. C., preferably <5.degree. C., particularly <2.degree. C., and the synthetic resin dispersion copolymer has a content of 0.05 to 2% by weight, preferably 0.1 to 0.4% by weight, particularly 0.05 to 0.2% by weight, based on the synthetic resin dispersion copolymer, of monomeric units derived from unsaturated hydrolyzable organic silicon compounds of the formula I, ##STR1## in which R denotes an organic radical olefinically unsaturated in the .omega.-position and R.sup.1 R.sup.2 and R.sup.3 which may be identical or different, denote halogen, preferably chlorine, or the group -OZ, Z denoting primary or secondary alkyl or acyl radicals optionally substituted by alkoxy groups, or hydrogen, the content of volatile non-aqueous constituents of the aqueous preparations being <0.1% by weight, preferably <0.05% by weight, based on the total non-volatile part, and the pH of the aqueous preparations being in the range from 5.5 to 10, preferably 7 to 9, particularly 8 to 9.

A preferred embodiment of the invention comprises the synthetic resin dispersion copolymer used containing monomeric units selected from the group vinyl esters, vinyl esters/ethylene, vinyl esters/vinyl chloride/ethylene, vinyl esters/vinyl versatates, vinyl esters/acrylic esters and acrylic esters/vinyl versatates/ethylene, in addition to monomeric units derived from compounds of the formula I.

Preferred compounds of the formula I are, for example, .gamma.-acryloxypropyltrimethoxysilane, .gamma.-methacryloxypropyltrimethoxysilane, vinyltrimethoxysilane, vinyltriethoxysilane, vinyltrimethylglycol silane, vinyltriacetoxysilane, vinyltrichlorosilane, vinylmethyldichlorosilane and .gamma.-methacryloxypropyltris(2-methoxyethoxy)silane.

A particular variant of the invention is for the synthetic resin dispersion copolymer used to comprise mixtures of dispersion copolymers, a part of which contains no monomeric units of the formula I and another part of which contains monomeric units of the formula I in such an amount that the mean content of monomeric units of the formula I in the total dispersion copolymer mixture is 0.05 to 2% by weight, preferably 0.1 to 0.4% by weight, particularly 0.05 to 0.2% by weight, based on the total synthetic resin dispersion copolymer mixture.

Furthermore, a particular feature according to the invention is that the aqueous preparations according to the invention are free from readily volatile residual monomers, from low alcohols and from ammonia and/or volatile amines or from components which give rise by cleavage to H.sub.2 S or mercaptans, if appropriate, and the total content of volatile non-aqueous constituents of the aqueous preparations is <0.05% by weight, based on the total non-volatile part.

The preparation of synthetic resin copolymer dispersions, where the monomers are copolymerized with hydrolyzable, unsaturated organic silicon compounds of the formula I, is known.

Synthetic resin dispersions based on vinyl acetate with 0.5. to .1% by weight, based on the total amount of monomers, of a copolymerizable silane, such as, for example, vinyltrimethoxysilane, .gamma.-methacryloxypropyltrimethoxysilane and vinyl tris(2-methoxyethoxy)silane, are known from U.S. Pat. No. 3,729,438. The polymer crosslinks on drying, giving rise to a clear, high-gloss film.

U.S. Pat. No. 3,814,716 describes synthetic resin dispersions based on vinyl acetate, acrylic esters, maleic and fumaric esters with 0.5 to 5% by weight of a copolymerizable silane. On drying the synthetic resin dispersion yields clear, high-gloss and crosslinked films with excellent water and solvent resistance.

The use of polymeric binders in aqueous dispersion for the preparation of structural coating materials are known from DE-PS 2,148,457, where the synthetic resin dispersions contain polymers from vinyl esters, acrylic esters or butadienestyrene copolymers into which the silanol groups have been introduced by polymerization.

The preparation of aqueous synthetic resin dispersions based on vinyl esters of carboxylic acids of 2 to 18 carbon atoms, ethylene, optionally up to 25% by weight of other olefinically unsaturated monomers and 0.3 to 5% by weight, based on the total amount of monomers, of an unsaturated hydrolyzable organic silicon compound, is known from DE-PS 2,148,458. Films prepared from the synthetic resin dispersions described exhibit with copolymers containing 1 to 2% by weight of the silicon compounds named above, high drying and wet peeling strengths on glass and asbestos cement. However, the synthetic resin dispersion prepared according to Example 1 of the above DE-PS possesses a 0.2% by weight content of unreacted monomeric vinyl acetate and the synthetic resin dispersions prepared according to Examples 6 and 10 contain, respectively, 3.8 and 4.8% by weight of methanol, in each case based on the polymeric part.

It cannot be simply assumed or deduced from the above state of the art that synthetic resin dispersions containing silanol groups may also give rise, in addition to a high pigment binding power in dispersion paints, to an improvement of the pull-off resistance of the coatings produced by the paints and, in addition, to a low tendency to soiling and blocking of the films or coatings produced therefrom, despite a low Tg and a low MFT.

It was therefore the more surprising to find that with binders based on synthetic resin dispersions having a low MFT, in the absence of volatile organic film-forming auxiliaries, a marked improvement of the binder properties is achieved if the dispersion copolymers contain only very small amounts of monomeric units with silanol groups formed from compounds of the formula I, amounts from 0.1 to 0.4% by weight, based on the total amount of monomer, being preferred.

A preferred embodiment of the present invention further is that the synthetic resin dispersion copolymer contained in the aqueous preparations and carrying silicon radicals in the monomeric units of the formula I was prepared by radically initiated copolymerization of the finely divided monomers having an amount of 0.05 to 2% by weight, preferably 0.1 to 0.4% by weight, particularly 0.05 to 0.2% by weight, based on the total amount of monomer, of monomers of the formula I in aqueous medium with the simultaneous use of hydroxyethylcellulose, non-ionic emulsifiers and monomeric sodium vinylsulfonate as emulsifier/protective colloid system, and the volatile alcohol components which may have formed by hydrolysis from the monomeric units of the formula I in the aqueous dispersion and any volatile amounts of residual monomers which may be present after the terminated polymerization reaction have been removed by physical methods, preferably by distillation under reduced pressure.

In the preparation of the synthetic resin dispersion copolymers, for example by emulsion polymerization, the alkoxy, acyloxy and halogen radicals of the silicon compounds of the formula I used hydrolyze at least partially to give silicon compounds containing hydroxyl groups (silanol groups) which are then contained in the copolymer and may lead to crosslinking between the macromolecules.

Suitable hydrolyzable unsaturated organic silicon compounds of the formula I are preferably those in which the radical R in the formula I represents an .omega.-unsaturated alkenyl of 2 to 10 carbon atoms, particularly of 2 to 4 carbon atoms, or an .omega.-unsaturated carboxylic acid ester formed from unsaturated carboxylic acids of up to 4 carbon atoms and alcohols carrying the Si group of up to 6 carbon atoms. Suitable radicals R.sup.1, R.sup.2, R.sup.3 are preferably halogen, particularly chlorine, and the group -OZ, Z representing primary and/or secondary alkyl radicals of up to 10 carbon atoms, preferably up to 4 carbon atoms, or alkyl radicals substituted by alkoxy groups, preferably of up to 3 carbon atoms, or acyl radicals of up to 6 carbon atoms, preferably of up to 3 carbon atoms, or hydrogen.

Examples of such compounds of the formula I are vinyltrichlorosilane, vinylmethyldichlorosilane, .gamma.-methacryloxypropyltris(2-methoxyethoxy)silane, vinylmethoxysilane, vinyltriethoxysilane, vinyldiethoxysilanol, vinylethoxysilanediol, allyltriethoxysilane, vinyltripropoxysilane, vinyltriisopropoxysilane, vinyltributoxysilane, vinyltriacetoxysilane, trimethylglycolvinylsilane, .gamma.-methacryloxypropyltrimethylglycolsilane, .gamma.-acryloxypropyltriethoxysilane and .gamma.-methacryloxypropyltrimethoxysilane.

The removal of residual monomers in the synthetic resin copolymer dispersions used according to the invention may also be carried out by resorting to known chemical methods such as, for example, by radically initiated, preferably using redox catalysts, secondary polymerization. Should subsequently traces of volatile monomers be still present in the dispersion, these can be readily removed by other methods, preferably by physical methods, particularly by distillation, preferably under reduced pressure and, if desired, by passing inert carrier gases such as, for example, air, nitrogen, CO.sub.2 or steam, through or over the reaction mixture.

A particular feature of the present invention is also the fact that the synthetic resin copolymer dispersions used according to the invention are not only free from volatile residual monomers, but also that any volatile alcohols forming or formed in the hydrolysis of the used comonomers of the formula I, such as, for example, methanol, methoxyethanol or isopropanol, have been removed by the aftertreatment referred to above using chemical and/or physical methods. This may be of considerable significance when, for example, vinyltrimethoxysilane is used as comonomer, since the methanol formed by hydrolysis and present in the resultant dispersion may prevent the use of the dispersion on toxicological grounds, if the methanol has not been eliminated beforehand.

The aqueous preparations according to the invention comprise in their final composition to be used as construction protective materials or structural materials, if appropriate, preferably also the following components as further auxiliaries in addition to the constituents from the synthetic resin copolymer dispersion:

0.1 to 0.6% by weight of a wetting agent or dispersant for filler and pigment,

0.1 to 1% by weight of a thickener,

0.01 to 2% by weight of a preservative and

0.001 to 0.5% by weight of an anti-foam,

each based on the total weight of the aqueous preparations.

The aqueous preparations according to the invention in the form of dispersion paints, coating materials and synthetic resin dispersion plasters, using synthetic resin dispersion copolymer latices according to the invention, which preparations are free from residual monomers and other volatile constituents, may be prepared by application of known techniques, such as they are used in the preparation of conventional products of this type using conventional synthetic polymer latices. However, it is important that in the choice of the usual starting materials attention is paid particularly to their freedom from ammonia, amines, ammonium compounds, alkyl ammonium compounds, solvents, H.sub.2 S, SO.sub.2 and formaldehyde as well as freedom from other volatile organic substances.

Preferred fillers used are, for example, calcium carbonate, magnesite, dolomite, kaolin, mica, talc, silica, calcium sulfate, feldspar, barium sulfate and plastic beads.

Examples of white pigments used are zinc oxide, zinc sulfide, basic lead carbonate, antimony trioxide, lithopone (zinc sulfide+barium sulfate) and, preferably, titanium dioxide.

Examples of inorganic colored pigments which may preferably be used are iron oxides, carbon black, graphite, luminescent pigments, zinc yellow, zinc green, Paris blue, ultramarine, manganese black, antimony black, manganese violet or Schweinfurt green.

Suitable organic colored pigments preferably are, for example, sepia, gamboge, Cassel brown, toluidine red, para red, Hansa yellow, indigo, azo dyes, anthraquinone and indigo dyes as well as dioxazine, quinacridone, phthalocyanin, isoindolinone and metal complex pigments of the azomethine series.

The fillers may be used as individual components. Mixtures of fillers such as, for example, calcium carbonate/kaolin and calcium carbonate/kaolin/talc have been found to be particularly useful in practice. To increase the hiding power and to save on titanium dioxide, finely divided fillers such as, for example, finely divided calcium carbonate and mixtures of various calcium carbonates with different particle size distribution are frequently used.

To adjust the hiding power, the shade and the depth of color the fillers are mixed with appropriate amounts of white pigment and inorganic and/or organic colored pigments.

To disperse the fillers and pigments in water, 0.1 to 0.6% by weight, based on the total weight of the aqueous preparation, of auxiliaries based on anionic or non-ionic wetting agents, such as preferably, for example, sodium pyrophosphate, sodium polyphosphate, naphthalenesulfonate, sodium polyacrylate, sodium polymaleinates and polyphosphonates such as sodium 1-hydroxyethane-1,1-diphosphonate and sodium nitrilotris(methylenephosphonate), may be added.

Thickeners which may be used, are inter alia preferably cellulose derivates such as methylcellulose, hydroxyethylcellulose and carboxymethylcellulose. Other thickeners which may be used, are casein, gum arabic, gum tragacanth, starch, sodium alginate, polyvinyl alcohol, polyvinylpyrrolidone, sodium polyacrylate and water-soluble copolymers based on acrylic and methacrylic acid, such as acrylic acid/acrylamide and methacrylic acid/acrylic ester copolymers.

Inorganic thickeners, such as, for example, bentonites or hectorite, may also be used.

Such thickeners are generally employed in amounts from 0.1 to 3% by weight, preferably 0.1 to 1% by weight, based on the total weight of the aqueous preparations.

The thickener may be incorporated already during the dispersion of the fillers and pigments in water with the addition of a dispersant and, if desired, an antifoam, for example using a dissolver; however, the thickener may also be added to the finished preparation, provided that the water balance of the finished construction protective material permits this to be done.

The synthetic resin copolymer dispersion used as binder according to the invention may already be present during the dispersion of the pigment and filler, but in most cases it is advantageously added to the filler/pigment paste which is still hot or also cooled, under rapid or also slower stirring. In order to maintain a pigment volume concentration of >60%, 4 to 35 parts by weight of synthetic resin dispersion copolymer are used per 65 to 95.9 parts by weight of filler+pigment.

The preparation of the copolymer dispersions for the aqueous construction protective material preparations low in noxious substances emission according to the invention is carried out in known manner, preferably by emulsion polymerization in the presence of a radically initiated catalyst and at least one emulsifier at a pH of 2 to 6. The various known catalysts forming free radicals or also redox systems may be used as catalysts. The concentration range of the total amount of emulsifiers is preferably between 0.5 and 5% by weight, based on the total amount of monomer, where the emulsifiers may be anionic, non-ionic or, if appropriate, cationic emulsifiers. It is also possible to use latex stabilizers, such as, for example, water-soluble polymers selected from the group carboxymethylcellulose, hydroxyethylcellulose, polyvinylpyrrolidone, poly-N-vinylacetamide, polyvinyl alcohol as well as combinations of emulsifiers and latex stabilizers, and also the known stabilizing comonomers based on monocarboxylic and dicarboxylic acids and the half-esters and amides thereof as well as vinylsulfonic acid and its salts.

Examples of monomers which are suitable for the preparation of the synthetic resin dispersion, are vinyl esters, in particular vinyl esters of aliphatic monocarboxylic acids of 1 to 12 carbon atoms, for example vinyl esters of lower (C.sub.1 -C.sub.6)carboxylic acids such as vinyl acetate, vinyl propionate, vinyl butyrate, vinyl caproate, furthermore vinyl laurate, vinyl decanate and vinyl versatate, furthermore, for example, olefinically unsaturated compounds of the formula II, ##STR2## in which R.sup.1 denotes hydrogen, an alkyl radical of 1 to 4 carbon atoms, an alkoxy radical of 1 to 4 carbon atoms, a nitrile group, a halogen atom, preferably chlorine, or an alkoxycarbonyl radical of 2 to 12, preferably 2 to 9, carbon atoms, and R.sup.2 represents hydrogen, a methyl or a vinyl group.

Examples of suitable monomers of the formula II are in particular olefins, for example ethylene and isobutylene, vinyl ethers, for example vinyl methyl ether, vinyl ethyl ether and vinyl n-butyl ether, furthermore acrylonitrile, methacrylonitrile, vinyl chloride, acrylic acid esters of monohydric alcohols, for example methyl acrylate, ethyl acrylate, butyl acrylate and 2-ethylhexyl acrylate, as well as methacrylic acid esters of monohydric alkanols, for example methyl methacrylate, ethyl methacrylate, butyl methacrylate and 2-ethylhexyl methacrylate. Equally suitable are maleic acid diesters, in particular of monohydric aliphatic alcohols of 2 to 10, preferably 3 to 8 carbon atoms, for example dibutyl maleate, dihexyl maleate and dioctyl maleate.

The monomers or monomer mixtures are chosen in such a manner that homopolymer-based, copolymer-based or terpolymer-based synthetic resin dispersions having an MFT of .ltoreq.10.degree. C., preferably .ltoreq.5.degree. C., particularly .ltoreq.0.degree. C., are produced. Any person skilled in the art knows on the basis of the Tg of the polymers and the polymerization parameters which monomers or mixtures of monomers must be employed for this purpose. Since the MFT below 0.degree. C. can no longer be measured, the lower limit of the MFT can only be specified by the Tg. In this connection the Tg should not be below -20.degree. C. preferably below -10.degree. C. Suitable copolymers are, for example, vinyl acetate/ethylene in the ratio 86/14 to 75/25, such as may be prepared at an ethylene pressure in the region from 25 to 60 bar. Other suitable copolymers are vinyl acetate/vinyl chloride/ethylene terpolymers in the ratio 58.8/25.2/16, prepared at an ethylene pressure of 40 bar and having an MFT of 10.degree. C., or 60.8/15.2/24 and 45 6/30 4/24, such as may be obtained at an ethylene pressure of 50 bar and having an MFT of <0.degree. C. and a Tg of -0.5 and +5.5.degree. C. respectively. With vinyl acetate/butyl acrylate copolymer dispersions the suitable MFT range is obtained when the monomers are used in the ratio 80/20 to 50/50.

The main monomers are copolymerized with small amounts, particularly preferably with 0.05 to 0.3% by weight, based on the total amount of monomer, of olefinically unsaturated silicon compounds of the formula I containing hydrolyzable groups, the radical R in the formula I preferably denoting vinyl, allyl, .gamma.-acryloxypropyl and .gamma.-methacryloxypropyl, and R.sup.1, R.sup.2, R.sup.3 preferably denoting alkoxy of 1 to 8 carbon atoms or alkoxyalkoxy of 2 to 10 carbon atoms, acetoxy or halogen, in particular chlorine.

Examples of particularly preferred compounds of the formula I are vinyltrimethoxysilane, vinyltriethoxysilane, vinyltrimethylglycolsilane, vinyltriacetoxysilane, .gamma.-acryloxypropyltrimethoxysilane, .gamma.-methacryloxypropyltrimethoxysilane, .gamma.-methacryloxypropyltris-(2-methoxyethoxy)silane, vinyltrichlorosilane, vinylmethyldichlorosilane and allyltrimethoxysilane.

The silanes of the formula I may be added in the emulsion copolymerization either mixed with the main monomers or separately. They may be metered in uniformly with the other monomers in the course of the polymerization or either in the first or the second half of the monomer amount. Only relatively small amounts of the above silanes are required to improve the properties of the synthetic resin dispersion according to the invention, preferably up to a maximum of 2% by weight, based on the total amount of monomers, preferably 0.1 to 0.4% by weight, particularly 0.05 to 0.2% by weight.

Removal of the unreacted monomers from the synthetic resin dispersion may be carried out chemically, i.e. for example by polymerization to completion. For this purpose catalysts forming free radicals are employed. Examples of such catalysts are peroxide and azo compounds, such as, for example, azobis(isobutyramidine hydrochloride). Equally particularly suitable are the combination types of catalysts in which both reducing agents and oxidation agents are used. When combination catalysts of this type are used, the reducing agent is generally termed activator and the oxidation agent initiator. Examples of suitable activators are bisulfites, sulfoxylates or compounds having reducing properties, such as, for example, ascorbic acid and ferrous salts. Examples of initiators are inter alia, hydrogen peroxide, persulfates such as sodium and potassium persulfate, perborates and also other pers compounds. Examples of special combination catalysts or redox systems which may be employed for the removal of the residual monomers by polymerization, are inter alia hydrogen peroxide and zinc formaldehyde sulfoxylate, hydrogen peroxide and sodium metabisulfite, sodium persulfate and sodium metabisulfite, hydrogen peroxide and sodium sulfite, hydrogen peroxide and rongalite, sodium or potassium persulfate and sodium sulfite, sodium or potassium persulfate and rongalite, hydrogen peroxide and ascorbic- acid, tert-butylhydroperoxide and sodium sulfite, tert-butylhydroperoxide and rongalite, sodium persulfate and sodium thiosulfate. Metal salts, used in traces, such as, for example, 1 to 100 ppm per monomer equivalent of iron or copper salts, such as, for example, Mohr's salt, may further activate the redox system. Examples are tert-butylhydroperoxide/Mohr's salt/rongalite or sodium persulfate/sodium sulfite/sodium thiosulfate/copper sulfate.

The redox catalyst is typically used in an amount between about 0.1 and about 2% by weight, preferably between about 0.25 and about 0.75% by weight, based on the amount of monomers. The activator is normally added in aqueous solution and the amount of activator generally is 0.25 to 1 times of the amount of initiator.

Physical methods, such as, for example, distillation, may also be used for the removal of residual monomers from the synthetic resin dispersion. Furthermore it is possible to combine chemical and physical methods. The removal of the residual monomers by distillation may take place under elevated, but preferably also under reduced pressure. In the removal of the residual monomers by distillation at 760 Torr or a lower pressure, the demonomerization may be speeded up by passing steam or a carrier gas, such as, for example, air, nitrogen or carbon dioxide, across the surface of the synthetic resin dispersion. However, the carrier gas is preferably passed in the demonomerization apparatus from the bottom through the synthetic resin dispersion. The residual monomers removed by physical methods from the synthetic resin dispersion are recovered by being condensed in a condenser. If a carrier gas is used in the demonomerization, coolants having a lower temperature than water from 0.degree. to 30.degree. C., for example cooling brine or acetone/dry ice, are employed if appropriate in the condenser. Furthermore, the residual monomers may be removed in vacuo and recovered from the synthetic resin dispersion by the use of pumps with rotary slide valves. The content of residual monomers and other volatile organic substances possibly originating from the starting materials or of volatile organic constituents formed in the polymerization, and of the alcohol which is formed in the hydrolysis of the copolymerized silicon compound of the formula I in the synthetic resin copolymer dispersion to be used according to the invention is less than 0.1% by weight, preferably 0.05 to 0.001% by weight, based on the dispersion copolymer.

Surprisingly in the case of binders having a low MFT, the copolymerization with tracers of copolymerizable silanes of the formula I gives rise to dispersion copolymers of a pigment binding power as great as that normally only achievable with dispersion (co)polymers having a high MFT, such as, for example, styrene/acrylate, when large amounts of solvent are added to the synthetic resin dispersion or to a dispersion paint prepared from it.

Synthetic resin copolymer dispersions based on vinyl acetate/ethylene and vinyl acetate/vinyl chloride/ethylene are preferably used for the odourless aqueous preparations, low in noxious substances emission, of construction protective materials, in addition to water, filler, pigment, dispersant, thickener, antifoam and preservative. To attain a low MFT, the ethylene pressure chosen must be higher in the case of vinyl acetate/vinyl chloride/ethylene than in the case of vinyl acetate/ethylene because of the higher freezing temperature of polyvinyl chloride. The resultant dispersion copolymers or the aqueous dispersions thereof have the advantage that copolymer dispersions may be made available which possess the low MFT required according to the invention.

Furthermore, because of the low boiling points of the monomers used, the synthetic resin dispersions prepared in this manner possess great advantages over styrene/acrylate and styrene/butadiene copolymers with their unpleasant by-products which may form, for example, by a Diels-Alder reaction.

The vinyl acetate/ethylene dispersion copolymers and the corresponding terpolymers with vinyl chloride may be advantageously prepared by copolymerization in water with the aid of anionic, non-ionic or cationic emulsifiers in the form of aqueous dispersions. Water-soluble, stabilizing polymers such as carboxymethylcellulose, hydroxyethylcellulose, polyvinylpyrrolidone, poly-N-vinylmethylacetamide and polyvinyl alcohol can be used for this purpose, as well as the known stabilizing comonomers based on monocarboxylic and dicarboxylic acids and their half-esters and amides. Furthermore, known initiator systems such as, for example persulfates, sodium persulfate/sulfite and tert-butylhydroperoxide/Fe.sup.2+ /rongalite may be advantageously used for the polymerization.

If the appropriate autoclaves are not available, such as are normally required for the copolymerization with ethylene and/or vinyl chloride, it is also possible to obtain dispersion copolymers according to the invention having the required MFT by copolymerization of customary monomers with those monomers that can strongly lower the MFT, such as, for example, 2-ethylhexyl acrylate, dioctyl maleate, vinyl versatate or butadiene. However, the copolymers and terpolymers based on vinyl acetate/ethylene and vinyl acetate/vinyl chloride/ethylene possess the quite considerable advantage that because of their low boiling points their starting monomers are readily freed from the residual monomer part which has not reacted in the polymerization.

By choosing appropriate technical measures, it is furthermore possible to use the recovered residual monomers for further polymerizations.

The above dispersion copolymers based on vinyl acetate/ethylene and vinyl acetate/vinyl chloride/ethylene with comonomers of the formula I are particularly preferred according to the invention.

By the combination of redox and strip processes or by the strip process alone for removing the residual monomers, the proposition is made here for the first time in connection with the preparation of low-emission construction protective materials according to the invention and the use of hydrolyzable and copolymerizable silanes of the formula I for the removal of mostly readily volatile alcohols formed in the hydrolysis of silanes. A special and preferred embodiment of the invention of unexpectedly great technical advance is based on the following mode of operation. Synthetic resin copolymer dispersions are prepared which contain, for example hydroxyethylcellulose or poly-N-vinylmethylacetamide as protective colloids and which contain in addition to these protective colloids preferably non-ionic emulsifiers and in addition to non-ionic emulsifiers only small amounts of ionic such as anionic or cationic emulsifiers. It is advantageous in this connection for further stabilization of the copolymer dispersion to use at the same time unsaturated hydrophilic comonomers capable of copolymerization, such as, for example, unsaturated monocarboxylic and dicarboxylic acids and their half-esters and amides as well as sodium methacrylamido-2-methyl-2-propanesulfonate or sodium vinylsulfonate. Synthetic resin copolymer dispersions are thus obtained with not very small particle sizes, such as, for example, .ltoreq.0.1 .mu.m, but with mean particle sizes of at least 0.1 .mu.m, preferably .gtoreq.0.15 .mu.m, particularly .gtoreq.0.2 .mu.m. They are distinguished by outstanding application properties, such as, for example, in that the synthetic resin dispersions are readily miscible with dry fillers and pigments and the construction protective materials prepared therefrom are highly resistant over the usual extended storage period.

For many years vain attempts were made by experts to prepare these dispersions, as advantageous on account of their application properties as those based on vinyl acetate/ethylene and vinyl acetate/vinyl chloride/ethylene and also possessing very high pigment binding power. This object has now been achieved in an unexpectedly advantageous manner by the present invention by the use of dispersion copolymers which contain comonomeric units derived from silicon compounds of the formula I, which units carry small amounts of hydrolyzable silicon-containing radicals or which form Si(OH).sub.x groups (x=1 to 3), and whose aqueous dispersions have an MFT of <10.degree. C. When these dispersion copolymers are used as binders in the aqueous preparations of construction protective materials under discussion, the so-called crazing of the dried coating and of the dried coating even after only a brief drying period of the preparation, as assessed by the resistance to washing and shearing of coatings according to DIN 53,778, surprisingly does not occur, despite the absence of solvents and film-consolidating auxiliaries, i.e the coating does not possess inadequate mechanical strength after a brief drying period, as can be frequently observed with paints derived from polymer dispersions.

Those aqueous preparations of construction protective materials according to the invention are particularly suitable and preferred which contain solvent-free synthetic resin copolymer dispersions having a low MFT as binders and whose copolymers contain in toto only small amounts of monomeric units derived from silicon compounds of the formula I, which units are capable of copolymerization and carry hydrolyzable silicon-containing radicals or form Si(OH).sub.x groups (x=1 to 3), viz. preferably 0.05 to 2% by weight, particularly 0.1 to 0.4, particularly preferably 0.05 to 0.2% by weight, based on the copolymer, and the copolymers were prepared by emulsion copolymerization from combinations of comonomers which result in the required low MFT values, in the presence of hydroxyethylcellulose, a non-ionic emulsifier, small amounts of monomeric vinyl sulfonate, with the addition in toto of only small amounts of comonomers of the formula I.

In order to tint dispersion paints and dispersion plasters, commercially available pigment pastes are frequently used. These pigment pastes generally contain solvents for reasons of stability or their preparability. A novel path has also been taken according to the invention for overcoming the resultant difficulties. Because of the high stability of the synthetic resin copolymer dispersion used according to the invention and its compatability with dry pigments, the preparation and use of pigment pastes containing solvents is unnecessary, since the pigment may be admixed with the synthetic resin dispersion or the white dispersion paint or the dispersion plaster in the dry state, if desired.

The advance in properties achievable in dispersion copolymers having MFT values of their aqueous dispersions of <10.degree. C