DE102006044144A1 - Non-reactive, chlorine-free composition - Google Patents

Abstract

The present invention relates to non-reactive compositions of A) amorphous poly-alpha-olefins which contain no organically bound chlorine and have a melting enthalpy in the range of 0 to 80 J / g, B) ketone, ketone / aldehyde and / or urea / Aldehyde resins and / or their hydrogenated derivatives, C) solvents and D) optionally auxiliaries and / or additives and their use as primers to improve the adhesion of coating materials such as paints, coatings, adhesives and sealants, inks and inks Plastics and glass.

Description

The The present invention relates to non-reactive compositions from A) amorphous poly-α-olefins, which contain no organically bound chlorine and a melting enthalpy in the range of 0 to 80 J / g, B) ketone, ketone / aldehyde and / or urea / aldehyde resins and / or their hydrogenated derivatives, C) solvents and D) optionally Auxiliary and / or additives and their use as primers for Improvement of the adhesion of coating materials such as Paints, varnishes, adhesives and sealants, inks and printing inks on plastics and glass.

It It is known that ketones or mixtures of ketones and aldehydes in the presence of basic catalysts or acids to resinous products can be implemented. Thus, mixtures of cyclohexanone and methylcyclohexanone Resins (Ullmann Bd. 12, p 551). The reaction of ketones and aldehydes mostly to hard resins, which are often used in the paint industry.

Technically significant ketone-aldehyde resins are nowadays mostly used made of formaldehyde.

Ketone-formaldehyde resins have been known for a long time. Process for the preparation are for. B. described in DE 10 2006 009 080.2 as well as in the patents cited therein.

to Usually, ketones and formaldehyde are produced in the presence reacted by bases with each other.

ketone, Ketone / aldehyde and / or urea / aldehyde resins and their hydrogenated Subsequent products are used in coating materials z. B. as a film-forming Additional components used to determine certain properties, such as drying rate, Shine, hardness or to improve scratch resistance. Because of their relatively low Molecular weights have conventional Ketone, ketone / aldehyde and / or urea / aldehyde resins and / or their hydrogenated secondary products have a low melt and solution viscosity and serve therefore in coating materials u. a. as film-forming functional fillers.

The Carbonyl groups of the ketone-aldehyde resins are subject to z. B. irradiation with z. B. sunlight classic degradation reactions such. From the Norrish Type I or II.

The use of unmodified ketone-aldehyde or ketone resins is therefore for high-quality applications such. B. outdoors, in which high resistance properties, in particular to weathering and heat are required, not possible. These disadvantages can be improved by hydrogenation of the carbonyl groups. The conversion of the carbonyl groups into secondary alcohols by hydrogenation of ketone-aldehyde resins has been practiced for a long time ( DE 870 022 ).

The preparation of carbonyl- and ring-hydrogenated ketone-aldehyde resins based on ketones containing aromatic groups is also possible. Such resins are used in DE 102006026758.3 or DE 12006026760.5 described.

Largely amorphous poly-α-olefins have long been known. Already in the DE-A-1 442 831 Catalyst systems are described which consist of the reaction product of a titanium trihalide with an aluminum compound on the one hand and a Titanoxykohlenwasserstoff on the other hand. Using this catalyst system, amorphous polyolefin copolymers are obtained.

From the DE-A-23 06 667 It is known that largely amorphous poly (1-butene) polymers by the low-pressure polymerization by polymerization of 1-butene, optionally in the presence of other olefins, at temperatures of 40 to 120 ° C in solution with the aid of a mixed contact of TiCl ₃ · n AlCl ₃ (n = 0.2 - 0.6) and a suitable trialkylaluminum.

In the DE-A-29 30 108 substantially amorphous butene-1-propene-ethene terpolymer of high softening point can be prepared in a similar manner, whereby also a mixed contact of TiCl ₃ · n AlCl ₃ (n = 0.3 to 0.35) and a trialkylaluminum as cocatalyst become.

In the DE-A-26 37 990 terpolymers are described which have a propene content of at least 93.2 wt .-% and an ethene content of at most 1.9 wt .-% and a 1-butene content of at most 4.9 wt .-%. Again, a TiCl ₃ mixed contact as well as a cocatalyst called an "activator" are used set.

In none of these applications is based on the use of primer compositions based on poly-α-olefins and ketone, ketone / aldehyde and / or urea / aldehyde resins and / or their hydrogenated secondary products pointed out that a very good adhesion of coating materials on untreated plastics.

to Coating non-polar plastics are usually pretreated, sufficiently high adhesion of the coating to the plastic to obtain. So z. B. plastics from polyolefins such. Polypropylene (PP), modified polypropylene (e.g., polypropylene-ethylene copolymers), polyethylene (PE), modified PE, mixtures such. B. Polypropylene / Ethylene-Propylene-Diene Blends (PP / EPDM) with low EPDM content, PP / PE blends or special polyester pretreated by certain methods, so that the coating material adheres to the plastic. Typical methods are flaming, corona discharge, gas phase fluorination or plasma treatment. By these methods, the plastic surface is partially oxidized, so that the surface tension increases. This allows subsequent Coatings or bonds to the substrate intermolecular Interact, thereby improving adhesion. The Disadvantages of these methods lie in the high costs and in the fact that the effect of pretreatment over a relatively small period of time (a few days to weeks). Furthermore corona-pretreated plastics tend to block, so that this pretreatment method is principally only inline to the application the coating material can take place.

Other Methods, such. B. the addition of additives to improve the liability during the Production of the plastic are also possible. The disadvantages of such Methods lie in the relatively high costs and in the reason that the lower molecular weight aggregates production problems of the plastic and the physical properties like z. B. can negatively affect the mechanical strength.

A different possibility The pretreatment offers the application of primers on the plastic before the application of the coating material.

In US 2003/055163 Binder compositions are described which contain, inter alia, chlorinated, COOH-containing polyolefins and ketone resins.

In JP 46027878 Also described are compositions containing, in addition to ketone resins, chlorinated polyolefins.

Products, which contain organically bound chlorine, can split off hydrochloric acid and in their Combustion z. B. form highly toxic dioxins. Therefore, such Methods for reasons of occupational and environmental protection not recommended.

The The object of the present invention was to provide compositions based on poly-α-olefins and ketone, ketone / aldehyde and / or urea / aldehyde resins and / or to find their hydrogenated derivatives, which has a very good adhesion of coating materials on untreated plastics. The compositions should be chlorine free and fast Drying and have a high blocking resistance. The effect The pretreatment should also be over a long period of time persist, allowing either a pretreatment directly after the production of the plastic by the plastic manufacturer (Off-line) or pretreatment directly in front of the application of the coating material (in-line) is possible.

The The object underlying the invention is surprisingly achieved according to the claims by before application of the coating material primer compositions based on poly-α-olefins and ketone, ketone / aldehyde and / or urea / aldehyde resins and / or whose hydrogenated derivatives are applied to the plastic, the following in more detail to be discribed.

The Compositions of the invention are in contrast to the state of the art free of organically bound Chlorine. They have a fast drying and a high blocking resistance on. The effect of the pretreatment is also constant over a long period of time.

The Compositions of the invention can therefore be used, in particular to improve adhesion of coating materials on plastics.

• A) 1 bis 98 Gew.-% mindestens eines nicht reaktiven Poly-α-olefins, das kein organisch gebundenes Chlor enthält und eine Schmelzenthalpie im Bereich von 0 bis 80 J/g aufweist und
• B) 1 bis 98 Gew.-% mindestens eines Keton-, Keton/Aldehyd- und/oder Harnstoff/Aldehyd-Harzes und/oder dessen hydrierten Folgeproduktes und
• C) 1 bis 98 Gew.-% mindestens eines Lösemittels und gegebenenfalls
• D) bis zu 97 Gew.-% mindestens eines Hilfs- oder Zusatzstoffes,

wobei die Summe der Gewichtsangaben der Komponenten A) bis D) 100 Gew.-% beträgt.The present invention relates to non-reactive compositions containing no organically bound chlorine, essentially containing

• A) 1 to 98 wt .-% of at least one non-reactive poly-α-olefin, which contains no organically bound chlorine and has a melting enthalpy in the range of 0 to 80 J / g, and
• B) 1 to 98 wt .-% of at least one ketone, ketone / aldehyde and / or urea / aldehyde resin and / or its hydrogenated secondary product and
• C) 1 to 98 wt .-% of at least one solvent and optionally
• D) up to 97% by weight of at least one auxiliary or additive,

wherein the sum of the weights of components A) to D) is 100 wt .-%.

It It was found that the combination of the below described Compositions of components A) to D) all required Fulfill criteria.

Component A)

The Invention essential component A) is used in amounts of 1 to 98 Wt .-%, preferably from 1 to 49 wt .-%, particularly preferably 1 to 40 wt .-% used. in principle suitable are all soluble in organic solvents and / or swellable Poly-α-olefins. These poly-α-olefins can by modification (eg with maleic anhydride) functional groups wear or be largely free of functional groups (pure Hydrocarbon polymers).

When Component A) are non-reactive, poly-α-olefins used which no contain organically bound chlorine and have a melting enthalpy in the Range from 0 to 80 J / g, which are therefore largely amorphous.

• • ein gewichtsmittleres Molekulargewicht von 2 000 bis 500 000 g/mol, bevorzugt 5 000 bis 300 000 g/mol, besonders bevorzugt 7 500 bis 200 000 g/mol,
• • eine Polydispersität PD von 2,0 bis 60, bevorzugt 2,5 bis 40, besonders bevorzugt 2,5 bis 30,
• • eine Glasübergangstemperatur Tg von –80 bis 0°C, bevorzugt –60 bis 0°C, besonders bevorzugt –55 bis –10°C,
• • eine Schmelzenthalpie im Bereich von 0 bis 80 J/g, bevorzugt im Bereich von 1 bis 70 J/g, besonders bevorzugt im Bereich von 1 bis 60 J/g sowie
• • eine weitgehende Löslichkeit oder Quellbarkeit in unpolaren Lösemitteln aufweist.

The non-reactive, largely amorphous poly-α-olefin may be a homo- or copolymer, for. Atactic polypropylene (APP), atactic polybutene (1) or preferably a co- and / or terpolymer having the following monomer composition:
From 0.5 to 100% by weight, preferably from 1 to 99% by weight, particularly preferably from 10 to 98% by weight, of one or more α-olefins having from 4 to 20 carbon atoms,
1 to 99.5 wt .-%, preferably 1 to 99 wt .-%, particularly preferably 2 to 90 wt .-% of propene and
0 to 50% by weight, preferably 0 to 20% by weight of ethene,
where the poly-α-olefin

• A weight-average molecular weight of from 2,000 to 500,000 g / mol, preferably from 5,000 to 300,000 g / mol, more preferably from 7,500 to 200,000 g / mol,
• A polydispersity PD of 2.0 to 60, preferably 2.5 to 40, particularly preferably 2.5 to 30,
• A glass transition temperature Tg of -80 to 0 ° C, preferably -60 to 0 ° C, particularly preferably -55 to -10 ° C,
• A melting enthalpy in the range of 0 to 80 J / g, preferably in the range of 1 to 70 J / g, particularly preferably in the range of 1 to 60 J / g and
• • has a high solubility or swellability in non-polar solvents.

there can the properties of poly-α-olefins all possible Assume variations within the above values, e.g. Legs PD from 2.5 to 30 (smallest range) and a Tg from -80 to 0 ° C (largest area).

As α-olefin with 4 to 20 carbon atoms are preferably 1-butene, 1-pentene, 1-hexene, 1-octene, 1-decene, 1-dodecene, 1-octadecene, 3-methyl-1-butene Methylpentene such. 4-methyl-1-pentene, a methylhexene or a Methylhepten, used alone or in mixture.

The determination of the molecular weight and polydispersity is carried out by high-temperature GPC. The determination is carried out according to ASTM D6474-99, but at a higher temperature (160 ° C instead of 140 ° C) and a lower injection volume of 150 μl instead of 300 μl. The solvent used is trichlorobenzene. The measurement takes place at a column temperature of 160 ° C. The universal calibration used for the evaluation of the elution curves is carried out on the basis of polyolefin standards. The results are not comparable with measurements whose calibrations are based on polymers of a different nature - z. B. on polystyrene basis - was carried out, or which have been done without universal calibration, otherwise there is an impermissible comparison of different three-dimensional polymer structures or hydrodynamic radii. Also, the comparison with measurements using other than the specified solvent, is not allowed, since in different solvents different three-dimensional polymer structures or hydrodynamic radii may be present, leading to a different result in the molecular weight determination.

The polydispersity PD is a ratio of number average and weight average molecular weight Are defined. It is particularly a measure of the width of the present Molar mass distribution, in turn, conclusions about the present polymerization behavior and the catalyst used. In addition, it is also a measure of the existing low molecular weight fraction, which in turn influences the adhesion properties has the polymer materials. The polydispersity is within certain limits for a particular Catalyst-cocatalyst combination characteristic. The molecular weight distribution Depending on the method used (eg 1, 2 or more stirred tank or combinations of stirred tank and flow tube) or reaction (Single or multiple dosing of catalyst, cocatalyst and monomers) either mono-, bi- or multimodal. The polydispersity has one relatively strong influence on the tack of the material at room temperature as well as liability.

Furthermore have molecular weight and polydispersity u. a. a strong influence on solution viscosity, mechanical Properties as well as adhesion properties. The lower the molecular weight is, the lower the viscosity in solution. However, mechanical Low molecular weight properties adversely affected be. To achieve optimum properties, therefore, is the weight average Molecular weight of component A) between 2,000 and 500,000 g / mol, preferably between 5,000 and 300,000 g / mol, more preferably between 7 500 and 200 000 g / mol and the polydispersity between 2.0 and 60, preferably between 2.5 and 40, more preferably between 2.5 and 30.

The Determination of the enthalpy of fusion, the glass transition temperature and the Melting range of the crystalline portion is by differential calorimetry (DSC) according to DIN 53 765 from the 2nd heating curve at a heating rate of 10 K / min. Of the Turning point of the heat flow curve is called the glass transition temperature evaluated. The glass transition temperature Eats in a known way control the monomer composition and the reaction conditions. Generally leads the use of longer chain Monomers to lower glass transition temperatures. Likewise lead Reaction conditions, which also form shorter-chain polymers (For example, relatively high polymerization temperatures) in one certain framework also for lowering the glass transition temperature.

A low glass transition temperature Tg has a positive effect on the (low temperature) flexibility, but has a negative effect on the blocking resistance and a fast drying rate (solvent retention time).

Therefore the Tg of component A) is chosen to be between -80 and 0 ° C, preferred between -60 and 0 ° C, more preferably between -55 and -10 ° C.

The Enamel enthalpy is a measure of the crystallinity of the polymer. The polymers of component A) have a relatively low crystallinity, i. H. they are largely, but not completely, amorphous. It is a certain crystallinity available for the required material properties is essential. The at Melting detectable crystalline areas extend over one huge Temperature range from 0 to 175 ° C and are of their intensity depending on the situation differently pronounced. The polymers of the component A) are characterized in their crystallinity by the occurrence of both mono- as well as bi- and multimodal melting peaks, which are used for Part are sharply separated, partly merge into each other. The enthalpy of fusion (as a standard for the total crystallinity) the polymer of component A) is between 0 J / g and 80 J / g, preferably in the range of 1 to 70 J / g, more preferably in the range from 1 to 60 J / g.

By the low crystallinity on the one hand a high transparency, on the other hand a special combination be achieved by advantageous material properties. Low crystalline polyolefins show a relatively high surface tack (Adhesion) at room temperature. As a result, they have a more flexible overall mechanical behavior on. However, the cohesion is such Materials are relatively low, which is why these low crystallinities are not generally desired. Due to the higher crystallinity one can achieved special combination of advantageous material properties become. Inventive polymers with relatively high crystallinities, such as B. polybutene or good copolymers with high butene shares, have z. B. very good tensile strength. Show at the same time they have a relatively low surface tack.

The solubility and / or swellability in nonpolar solvents is desired so that the component A) can be processed. For one thing, she should be in Combination with components B) to D) be homogeneously miscible, on the other hand, the composition of A) to D) should be prepared by conventional methods, such as As spraying, printing, pouring, brushing or application by sponge, easy to apply.

The solubility is determined by solving the component A) in the respective solvent or solvent mixture in 10 or 50% dilution with stirring at reflux temperature and then cooling the solution to room temperature. The solubility of component A) in xylene is between 80 and 99.9%, preferably between 85 and 99.5%, and more preferably between 90 and 99.0 %. About that In addition, component A) is soluble in aromatic solvents such as As toluene, benzene, cresols, naphthalene, tetrahydronaphthalene and / or in aliphatic solvents and solvent mixtures, such as decahydronaphthalene, hexane, heptane, cyclohexane, crystal oils, white spirits, Turpentine, paraffins alone or in mixture.

Typical methods of preparation and compositions for preparing the non-reactive, substantially amorphous, poly-α-olefins are e.g. B. described in DE 40 00 695 . DE 100 31 293 and WO 2006/060648 ,

Component B)

The Invention essential component B) is used in amounts of 1 to 98 Wt .-%, preferably from 1 to 49 wt .-%, particularly preferably 1 to 40 wt .-% used.

These Products are especially for a fast drying rate (improved solvent retention) and a high blocking resistance. Furthermore becomes by the use of the components B) the compatibility to subsequent coating materials in the wet-on-wet application and the adhesion of the subsequent coatings on the primer layer improved. Last but not least, the solubility of component A) the composition of the invention increased by the presence of component B) and the course and the solids content improved.

When Component B) are suitable ketone, ketone / aldehyde and / or urea / aldehyde resins and their hydrogenated derivatives alone or in mixture.

in the Generally can all in the literature for Ketone and ketone-aldehyde resin syntheses as suitably named ketones, usually all C-H-acidic ketones are used.

When Ketones for the preparation of ketone and ketone-aldehyde resins (component B)), all ketones, in particular acetone, acetophenone, methyl ethyl ketone, tert-butyl methyl ketone, heptanone-2, pentanone-3, methyl isobutyl ketone, Cyclopentanone, cyclododecanone, mixtures of 2,2,4- and 2,4,4-trimethylcyclopentanone, Cycloheptanone and cyclooctanone, cyclohexanone and all alkyl-substituted ones Cyclohexanones having one or more alkyl radicals, in total Have 1 to 8 hydrocarbon atoms, individually or in mixture. As examples of alkyl-substituted cyclohexanones, 4-tert-amylcyclohexanone, 2-sec-butylcyclohexanone, 2-tert-butylcyclohexanone, 4-tert-butylcyclohexanone, 2-methylcyclohexanone and 3,3,5-trimethylcyclohexanone.

Prefers are ketone-aldehyde resins based on the ketones acetophenone, cyclohexanone, 4-tert-butylcyclohexanone, 3,3,5-trimethylcyclohexanone and heptanone, alone or in admixture and ketone resins based on cyclohexanone.

When Aldehyde component of the ketone-aldehyde resins (component B)) are suitable in principle unbranched or branched aldehydes, such as. B. Formaldehyde, acetaldehyde, n-butyraldehyde and / or isobutyraldehyde, Valeric aldehyde and dodecanal. In general, everyone can in the literature for Ketonharzsynthesen be used as suitable called aldehydes. Preferably, however, formaldehyde is used alone or in mixtures.

The needed Formaldehyde is usually as about 20 to 40 wt .-% aqueous or alcoholic (eg, methanol or butanol) solution. Other uses of formaldehyde such. B. also the use of para-formaldehyde or trioxane are also possible. in principle However, all formaldehyde donating compounds are suitable. aromatic Aldehydes, such as. As benzaldehyde, may in mixture with formaldehyde Also included.

Particularly preferred starting compounds for the ketone-aldehyde resins acetophenone, Cyclohexanone, 4-tert-butylcyclohexanone, 3,3,5-trimethylcyclohexanone and heptanone used alone or in mixture and formaldehyde.

The molar ratio between the ketone and the aldehyde component is between 1: 0.25 to 1:15, preferably between 1: 0.9 to 1: 5 and particularly preferred between 1: 0.95 to 1: 4.

Process for the preparation of the ketone-aldehyde resins are z. B. described in EP 1 486 520 . DE 102006009079.9 and DE 102006009080.2 and the literature quoted there.

Hydrogenated secondary products of the resins of ketone and aldehyde are also used as component B). The ketone-aldehyde resins described above are hydrogenated in the presence of a catalyst with hydrogen at pressures of up to 300 bar. The carbonyl group of the ketone-aldehyde resin is converted into a secondary hydroxy group. Depending on the reaction conditions, a part of the hydroxy groups can be split off, so that methylene groups result. To illustrate, the following scheme is used:

Process for the preparation of the hydrogenated products are z. B. described in DE 102006009079.9 and DE 102006009080.2 ,

In the case of ketones containing aromatic structural elements, depending on the hydrogenation conditions, these structural elements are also hydrogenated. Suitable resins are for. In DE 102006026760.5 and DE 102006026758.3 described.

in der X Sauerstoff oder Schwefel, A einen Alkylenrest bedeuten und n für 0 bis 3 steht, mit 1,9 (n + 1) bis 2,2 (n + 1) mol eines Aldehyds der allgemeinen Formel (ii)

in der R₁ und R₂ für Kohlenwasserstoffreste (z. B. Alkyl-, Aryl- und/oder Alkylarylreste) mit jeweils bis zu 20 Kohlenstoffatomen stehen und/oder Formaldehyd verwendet.As component B), furthermore, urea-aldehyde resins are used with the use of a urea of the general formula (i)

in which X is oxygen or sulfur, A is an alkylene radical and n is 0 to 3, with 1.9 (n + 1) to 2.2 (n + 1) mol of an aldehyde of the general formula (ii)

in which R ₁ and R _{2 are} hydrocarbon radicals (for example alkyl, aryl and / or alkylaryl radicals) in each case having up to 20 carbon atoms and / or formaldehyde is used.

suitable Urea of the general formula (i) with n = 0 are z. B. urea and thiourea, with n = 1 methylene diurea, ethylene diurea, Tetramethylenediurea and / or hexamethylenediurea as well their mixtures. Preference is given to urea.

suitable Aldehydes of the general formula (ii) are, for example, isobutyraldehyde, 2-methylpentanal, 2-ethylhexanal and 2-phenylpropanal and theirs Mixtures. Isobutyraldehyde is preferred.

formaldehyde can in aqueous Form, some or all of alcohols such. As methanol or ethanol may be used as paraformaldehyde and / or trioxane.

in the In general, all monomers used in the literature for the preparation of urea-aldehyde resins B) are described suitable. Particularly preferred are urea, Isobutyraldehyde and formaldehyde.

Typical methods of preparation and compositions are e.g. In DE 27 57 220 . DE-OS 27 57 176 such as EP 0 271 776 described. Commercial products are the Laropal ^® A81 or Laropal ^® A 101 from BASF AG.

• • eine Hydroxylzahl zwischen 0 und 450 mg KOH/g, bevorzugt zwischen 0 und 375 mg KOH/g, besonders bevorzugt zwischen 0 und 350 mg KOH/g,
• • eine Farbzahl nach Gardner (50 Gew.-% in Ethylacetat) zwischen 0 und 5, bevorzugt zwischen 0 und 3,0, besonders bevorzugt zwischen 0 und 2,0,
• • eine Farbzahl nach Gardner (50 Gew.-% in Ethylacetat) nach thermischer Belastung des Harzes (24 h, 150°C) zwischen 0 und 10,0, bevorzugt zwischen 0 und 7,5, besonders bevorzugt zwischen 0 und 5,0,
• • ein zahlenmittleres Molekulargewicht Mn von 300 bis 10.000 g/mol, bevorzugt von 400 bis 5.000 g/mol, besonders bevorzugt von 400 bis 3.000 g/mol,
• • eine Polydispersität (Mw/Mn) zwischen 1,25 und 4,0, besonders bevorzugt zwischen 1,3 und 3,5,
• • einen Schmelzpunkt/-bereich zwischen 20 und 180°C, bevorzugt zwischen 30 und 140°C, besonders bevorzugt zwischen 40 und 130°C und
• • eine Löslichkeit in unpolaren, organischen Lösemitteln.

Component B) is characterized by

• A hydroxyl number between 0 and 450 mg KOH / g, preferably between 0 and 375 mg KOH / g, more preferably between 0 and 350 mg KOH / g,
• Gardner color number (50% by weight in ethyl acetate) is between 0 and 5, preferably between 0 and 3.0, particularly preferably between 0 and 2.0,
• Gardner color number (50% by weight in ethyl acetate) after thermal loading of the resin (24 h, 150 ° C.) between 0 and 10.0, preferably between 0 and 7.5, particularly preferably between 0 and 5.0 .
• A number-average molecular weight Mn of from 300 to 10,000 g / mol, preferably from 400 to 5,000 g / mol, more preferably from 400 to 3,000 g / mol,
• A polydispersity (Mw / Mn) between 1.25 and 4.0, more preferably between 1.3 and 3.5,
• A melting point / range between 20 and 180 ° C, preferably between 30 and 140 ° C, more preferably between 40 and 130 ° C and
• • solubility in non-polar organic solvents.

Also Here the properties are freely variable.

The Hydroxyl number is a measure of the polarity of the resins. The higher it is at otherwise constant parameters of resin properties (eg, carbonyl number, molecular weight), the higher the polarity. To a good one compatibility to ensure component A) the hydroxyl number should be chosen so low that the solubility in nonpolar solvents given is. On the other hand, subsequent layers adhere better on the primer layer, the more polar the primer is. The optimum hydroxyl number is between 0 and 450 mg KOH / g, preferably between 0 and 375 mg KOH / g, more preferably between 0 and 350 mg KOH / g. The determination is based on DIN 53240-2 "Determination of the Hydroxyl Number" to ensure that an acetylation time of 3 h is maintained exactly becomes.

The Determination of Gardner color number is carried out in 50% strength by weight solution of Component B) in ethyl acetate on the basis of DIN ISO 4630 and is a measure of color of the resin. The lower the color number, the more colorless it is Resin. Also, in this way, the color number after thermal Determined load. This method can be used to create a Note on heat resistance of component B). For this purpose, component B) is first 24 h at 150 ° C in air atmosphere stored (see determination of non-volatile content). Then done the determination of Gardner color number in 50% strength by weight solution of thermally loaded resin in ethyl acetate on the basis of DIN ISO 4630. The smaller the color number, the more heat-resistant it is the resin.

The Measurement of molecular weight and polydispersity of the component B) by means of gel permeation chromatography in tetrahydrofuran against polystyrene as standard. The polydispersity (Mw / Mn) is calculated the relationship weight average (Mw) to number average (Mn).

ever higher that Molecular weight is the higher is the melting range of component B) and the better the drying rate, however, the higher the solution viscosity. Given Molecular weight (Mn), the solution viscosity is the higher, depending inconsistent the solved Polymer is (high polydispersity).

Ideally the number average molecular weight Mn is between 300 and 10 000 g / mol, preferably between 400 and 5000 g / mol, more preferably between 400 and 3,000 g / mol and the polydispersity (Mw / Mn) between 1.25 and 4.0, more preferably between 1.3 and 3.5.

One preferably high melting range of component B) is desirable so that z. B. the drying speed the composition according to the invention, the hardness and the blocking resistance of the coatings are as high as possible.

The determination is carried out with a Kapillarschmelzpunkt-meter (Büchi B-545) based on the DIN 53181. The preferred melting point / range of component B) is between 20 and 180 ° C, preferably between 30 and 140 ° C, more preferably between 40 and 130 ° C.

The solubility Component B) is in the usual organic solvents such as Ethyl acetate, butyl acetate, acetone, butanone, etc. are added.

Furthermore component B) is soluble in nonpolar solvents. This is mandatory because it only succeeds, the very non-polar component A) with the component B) to mix homogeneously.

The Component B) is soluble in aromatic solvents at 10% and 50% by weight dilution such as As xylenes, toluene, benzene, cresols, naphthalene, tetrahydronaphthalene and / or in aliphatic solvents and Solvent mixtures, such as decahydronaphthalene, hexane, heptane, (methyl) cyclohexane, crystal oils, white spirits, Turpentine, paraffins alone or in mixture.

Component C)

The Essential component C) is used in amounts of 1 to 98 Wt .-%, preferably from 2 to 98 wt .-%, particularly preferably 20 to Used 98 wt .-%.

When Component C) are generally suitable all organic solvents, which in the adhesive and Paint industry can be used.

Prefers be z. B. aromatic, aliphatic and / or cycloaliphatic solvent and solvent mixtures, such as As xylenes, toluene, benzene, cresols, naphthalene, tetrahydronaphthalene, Decahydronaphthalene, hexane, heptane, (methyl) cyclohexane, crystal oils, white spirits, Terpentine, paraffins alone or in mixture.

Component D)

The Component D) may optionally be included and is used in amounts of 0 to 97 wt .-% used. Suitable as component D) are auxiliary and additives such as inhibitors, other organic Solvents Water, surface-active Substances, such. Defoamer, Ventilator, Slip and leveling agents, substrate wetting agents, antiblocking agents, Oxygen and / or radical scavengers, Catalysts, light stabilizers, color lighteners, photosensitizers and initiators, additives for influencing rheological properties such as z. Thixotropic and / or thickening agents, skin preventatives, Antistatic agents, wetting and dispersing agents, crosslinking agents such. B. blocked or unblocked (poly) isocyanates, preservatives such as z. As well as fungicides and / or biocides, thermoplastic additives, Plasticizers, matting agents, fire retardants, internal release agents, Blowing agents and / or dyes, pigments and / or fillers.

Furthermore can as component D) in amounts of up to 40% by weight of further polymers, such as As polyurethanes, polyacrylates, polyethers, polyesters, alkyd resins, Polyamides, casein, cellulose ethers, derivatives of cellulose, polyvinyl alcohols and derivatives, polyvinyl acetates, polyvinylpyrolidones, rubbers, Natural resins, hydrocarbon resins such. Coumarone, indene, cyclopentadiene resins, Terpene resins, maleate resins, phenolic resins, phenolic / urea-aldehyde resins, Aminoplasts (eg melamine, benzoguanamine resins), epoxy acrylates, Epoxy resins, silicic acid esters and alkali silicates (eg water glass), silicone resins and / or fluorine-containing Polymers. These binders can foreign and / or self-crosslinking, air-drying (physically drying) and / or oxidatively curing.

Preparation of the compositions the components A) to D):

The Preparation of the compositions is carried out by intensive mixing of the components at temperatures of 20 to 80 ° C ("textbook of paint technology", Th. Brock, M. Groteklaes, P. Mischke, ed. V. Zorll, Vincentz Verlag, Hannover, 1998, page 229 ff.), If appropriate in an inert gas atmosphere. This is the component C) and the components A), B) and optionally D) are added.

The Compositions of the invention from the components A) to D) are free of chlorine. Chlorine free means that no chlorine-containing products containing organically bound chlorine included, such as As chlorinated rubbers, chlorinated polyolefins or the like, be used. Inorganic chlorides (eg salts), however, can be contained, these usually no toxicological potential have.

The invention also relates to the use of non-reactive compositions as Pri compositions for improving the adhesion to plastics, in particular to unpretreated plastics.

The Compositions of the invention from the components A) to D) can used as primer compositions, which is a very good Adhesion of adhesive, sealing and / or Enable coating materials on untreated plastics, so that usual Methods for the pretreatment of plastics such. B. flaming, the corona discharge, the plasma treatment or the gas phase fluorination omitted. It sufficient according to the simple previous cleaning of the substrates with typical cleaning agents such. B. iso-propanol and / or n-hexane out.

The compositions according to the invention of components A) to D) are particularly suitable as primers for improving the adhesion of adhesives, sealants and / or coating materials to unpretreated, low-energy plastics which have a surface tension below 40, preferably below 38, more preferably below 34 mN / m ² . However, it was surprising that the adhesion to glass was also improved.

When examples for Such low-energy plastics are polyolefins such z. B. polypropylene (PP), modified polypropylene, such as. Polypropylene-ethylene copolymers (e.g., block copolymers or random copolymers), Polyethylene (PE), modified PE, mixtures such. B. polypropylene / ethylene-propylene-diene blends (PP / EPDM) with low EPDM content, PP / PE blends, but also rubbers, Called Polyvinyichlorid or special polyester.

The Plastics can workpieces or shaped body be composites, such. As paper and / or aluminum laminations Plastic or foils.

The Plastics can in the commodity sector (eg bottles, cans, carrier bags, labels o. Ä.) or for high quality Applications (eg in the electronics industry, in the automotive or Aircraft construction) can be used.

The Compositions of the invention from the components A) to D) have a rapid drying and a high blocking resistance.

The Pretreatment effect will persist for a long time, so that optionally a pre-treatment directly after production the plastic at the plastic manufacturer (off-line) or a Pretreatment directly before the application of the coating material (In-line) possible is.

ever according to purpose, the following are applied to the primer layers according to the invention Adhesive, sealing or coating materials applied. The following Layer can be applied directly to the primer "wet-on-wet" are, i. the solvent will not be removed. It is also possible to use the primer first at room temperature or increased Temperature of the volatile Components and then the subsequent layer on the "dry" - i.e., solventless - primer to apply.

The Composition according to the invention can with usual Methods are applied to the plastic substrates. Examples therefor are u. a. (electrostatic) spraying, spraying, spincoating, Casting, diving, Drumming, flooding, rolling, wiping, washing, printing, rolling, brushing, Extrusion.

The Layer thickness of the primer layers according to the invention lies after evaporation of the volatile Ingredients such. B. solvents between 0.01 and 100 μm, preferably 0.1 and 30 μm, more preferably between 0.2 and 10 microns.

When Subsequent coating materials may be all coating materials be used, in particular all solvent-containing, aqueous Coating materials or solvent-free Coating materials (eg radiation-curable coating materials and / or powder coatings) such. As fillers, fillers, base and / or topcoats and printing inks, ballpoint pen pastes, inks, Polishes, glazes, laminations, heat sealing lacquers, cosmetics and / or sealing and insulating materials as well as adhesives.

Of the Course of the compositions according to the invention on the substrates and the course of the subsequent coating materials on the compositions of the invention is impeccable and the surfaces are free of disturbances, such as craters and wetting disorders.

object The invention also relates to objects prepared using the non-reactive compositions.

The The following examples are intended to illustrate the invention made but further do not restrict their scope:

I.) Component A): Preparation of the polyolefin

Using a mixed contact of a crystalline titanium trichloride in the form of an aluminum-reduced TiCl ₄ (TiCl ₃ · 0.33 AlCl ₃ ) and aluminum triisobutyl (in a weight ratio of 1: 4), the monomers indicated in Table 1 were dissolved in n-butane at the in Table 1 temperature polymerized in a laboratory autoclave, with hydrogen was used as molecular weight regulator. There were pressures of 15 to 35 bar. The monomers ethene and propene were added continuously during the reaction time of 3 h; the monomer 1-butene was submitted. After 3 h, the reaction mixture was added with isopropanol, whereby the reaction was stopped. In an evaporator unreacted monomers and the solvent n-butane were evaporated. The melt of the polyolefin was discharged at a temperature of about 190 ° C. Table 1. Reaction conditions and properties of polyolefins I-1 to I-3 ¹³ C-NMR reaction parameters properties Ex. monomer Content [% by weight] Reaction temperature [° C] H ₂ amount [standard liters] Tg [° C] Enthalpy of fusion [Y / g] M _w (g / mol) polydispersity I-1 Ethene propene 1-butene 4.5 66 29.5 100 8th -33 24.5 92,000 5.1 I-2 Propene 1-butene 70 30 100 20 -28 12.5 34,000 4.6 I-3 Ethene propene 1-butene 7 70 23 100 18 -36 15.5 35,000 4.4

The Polyolefins I-1 to I-3 are soluble in z. B. xylene.

II.) Component B)

1. Preparation of the ketone-aldehyde resin

The preparation of the ketone-aldehyde resin was carried out according to Example GL 254 of EP 1 486 520 A1 ,

2. Preparation of hydrogenated ketone-aldehyde resin

The preparation of the hydrogenated ketone-aldehyde resin was carried out according to Example 2 of DE 102006026758.3 ,

3. Preparation of the urea-aldehyde resin

The preparation of the urea-aldehyde resin was carried out according to Example 1 of DE 27 17 76 ,

The following Table 2 gives an overview of the properties of Resins II-1 to II-3 Table 2. Properties of Resins II-1 to II-3 Resin II-1 Resin II-2 Resin II-3 Hydroxyl number [mg KOH / g] 7.6 16.0 19.4 Melting point [° C] 63 49 63 Non-volatile content (24 h at 150 ° C) [% by mass] 78.2 99.6 64.3 Gardner color number (50% in ethyl acetate) 1.0 0.0 1.1 Gardner color number (after 24 h at 150 ° C, 50% in ethyl acetate) 3.9 0.2 3.2 Mn (GPC vs PS) [g · mol ^-1 ] 500 890 1550 Mw (GPC vs. PS) [g.mol ^-1 ] 670 1350 4640 polydispersity 1.3 1.5 3.0 Solubility (10% / 50%) white spirit clear / clear clear / clear clear / clear Isopar ^® H clear / clear clear / clear clear / clear n-hexane slightly cloudy / clear clear / clear slightly cloudy / clear xylene clear / clear clear / clear clear / clear

Preparation of primer compositions

The in the following Table 3 specified substances are dissolved with stirring and homogenized. This is the respective solvent (Component C)) and the polyolefin I-1 and the respective resin II-1 to II-3 slowly with stirring added at room temperature. To speed up the release is briefly with stirring to 60 ° C heated.

After dissolution, the solutions are filtered. Table 3. Composition of Control V1 and Primers P1 through P6 (all data in grams / g) V1 P1 P2 P3 P4 P5 P6 P7 P8 Polyolefin I-1 10.0 5.0 3.3 2 5.0 5.0 5.0 5.0 5.0 Resin II-1 - 5.0 6.7 8th 5.0 5.0 5.0 - - Resin II-2 - - - - - - - 5.0 - Resin II-3 - - - - - - - - 5.0 xylene 90.0 90.0 90.0 90.0 - - - 90.0 90.0 Solvesso ^® 100 - - - - 90.0 - - - - Shellsol ^® D40 - - - - - 90.0 - - - white spirit - - - - - - 90.0 - -

All solutions are clear to slightly cloudy, colorless to yellowish and water-thin. In the comparative solution V1 the proportion was more insoluble Ingredients relatively higher as in the compositions P1 to P8. This can be explained that the resins II-1 to II-3 act as a solubilizer.

The solutions V1 and P1 to P8 were knife-coated (2 μm wet layer) on films, the previously cleaned with ethanol and n-hexane. After evaporation of the solvents (different exhaust times, s. Tab. 4) was a printing ink by means of doctor (2 micron wet layer) applied to the films and at room temperature from the solvents freed.

The Assessment of the adhesive properties took place after the so-called Crumple test. For this purpose, the coated film was after 24 h after Successful application of the ink "wrinkled".

is the coating undamaged, the liability is very good (1). In case of injury the coating will the degree of injury assessed (2: minor flaking, ..., 6: complete Delamination).

It was also the adhesion was assessed by means of the tape tear-off method (Tesa test). For this purpose, an adhesive tape after different ventilation times the ink (5 min, 1 h, 24 h) glued to the ink film and subsequently demolished again. If the coating is undamaged, the adhesion is very high good (1). In case of damage to the coating, the degree of injury assessed (2: minor spalling, ..., 6: complete detachment).

A printing ink of the following composition was used:
39.0 g of ethanol
11.2 g of ethyl acetate
40.0 g of synthetic resin 1201 (Degussa AG)
7.2 g Hacolor blue 50423 (hawthorn)

The Ingredients were combined in the order given with stirring given and homogenized.

The following types were used as film substrates (plaster films):
Treofan NNA 40 (PP film), Hostaphan RN 50 (PET film), Genotherm EE 87 (PVC film)

In Tables 4-1 and 4-2 below are the results of the liability studies (Wrinkle test, Tesatest) of the inks on the respective primer P1 to P8 compared to the ink on the respective untreated Foil and shown on the comparison primer V1.

The adhesion of the ink to the respective plastic is poor without a primer layer. This is shown by the results of the wrinkle tests and the tesat tests. Only PVC will be slightly better Liability (Tesatest 3 after 24 h) found. Comparative experiment V1 shows that although a primer without component B) can fundamentally improve adhesion. However, a relative improvement is only observed after a flash off time of 2 minutes and is not at a very high level. In contrast, the adhesion of the printing ink on the plastic substrates is significantly improved already after short flash-off times by the primer layers according to the invention.

It it turns out that a higher Concentration of component B) (P1 to P3) positive on the adhesion after short flash off times effect. Since all of these primer coatings travels after 30 seconds are non-tacky, is also a high block resistance after the shortest Time guaranteed.

The Examples P4 to P6 show no significant compared to P1 Differences. The differences lie in the range of measuring accuracy the relative methods. Therefore, the influence of the solvent used is (Component C)) low.

The solutions V1 and P1 to P8 were knife coated (2 μm wet layer) on polyethylene and polypropylene panels the company Krüppel, which had been previously cleaned with ethanol and n-hexane applied. After evaporation of the solvents a printing ink was applied by means of a doctor blade (2 μm wet layer) and at RT of the solvent freed. Furthermore became a commercial one 2-component polyurethane paint by means of spray application Applied to the panels and over 30 min at 80 ° C dried.

The Evaluation of the adhesive properties of the printing inks was carried out by means of Tape tear-off method (Tesa test). For this purpose, an adhesive tape after different ventilation times the ink (5 min, 1 h, 24 h) glued to the ink film and subsequently demolished again. If the coating is undamaged, the adhesion is very high good (1). In case of damage to the coating, the degree of injury assessed (2: minor spalling, ..., 6: complete detachment).

at The applied paints were cross - hatched in Based on DIN EN ISO 2409 (GT 0 very good, GT 5 complete delamination).

The results are shown in Table 5. Table 5. Results of the adhesion tests of the 2-component paints (cross-cut test) and the printing inks (Tesa test) on the respective primer P1 to P8 in comparison to the paint on the respective untreated panel and on the comparative primer V1 sample Drying conditions of the primer crosshatch Tesa test PE PP PE PP 5 min 1 h 24 hours 5 min 1 h 24 hours without without primer (comparison) 5 5 6 6 6 6 6 6 V1 5 min RT 5 5 6 6 6 2-3 2 2 30 min 100 ° C 5 5 4-5 3 3 4-5 2-3 2-3 P1 5 min RT 5 2 4 3-4 3-4 1 1 1 30 min 100 ° C 2-3 0 1 1 1 1 1 1 P2 5 min RT 5 1 4-5 4 4 1 1 1 30 min 100 ° C 3 0-1 2 2 1-2 1 1 1 P3 5 min RT 5 2 5 4 4 1 1 1 30 min 100 ° C 3 1-2 2 2 1-2 1 1 1 P4 5 min RT 5 2 4-5 3 3-4 1 1 1 30 min 100 ° C 2-3 0 2 2 1 1 1 1 P5 5 min RT 5 2 4-5 3 3 1 1 1 30 min 100 ° C 2 0-1 1 1 1 1 1 1 P6 5 min RT 5 2 4 3 3 1 1 1 30 min 100 ° C 2-3 0-1 1-2 1 1 1 1 1 P7 5 min RT 5 3 4 4 4 1 1 1 30 min 100 ° C 4-5 2-3 2-3 2-3 2 1 1 1 P8 5 min RT 5 1-2 3 3 3 1 1 1 30 min 100 ° C 3 0 1-2 1 1 1 1 1

The adhesion of the 2-component polyurethane coating to the respective plastic is poor without a primer layer. The same results result from the pretreatment by means of comparative primer V1. In all cases there is no liability (crosscut GT 5). On PE, the adhesion is not improved by pretreatment using the inventive primer P1 to P8, when the primer was freed from the solvent at RT. If, however, the primers P1 to P8 according to the invention are freed from the solvent at elevated temperature, markedly improved adhesion results of the 2-component paint on PE result.

On PP improve the primers according to the invention P1 to P8 the adhesion of the paint excellent. In the trend draws However, here, too, that evaporation of the solvent at elevated Temperature can further improve the adhesion properties.

The Adhesion of the ink on the respective plastic is without one Primer layer also bad (Tesa test 6). The pretreatment of PE by means of V1 indicates after 5 min. evaporate off the solvents at RT no improvement. A slight improvement will be against it found after forced drying of the primer. PP will be easy Improvements found by the pretreatment by means of V1.

Become the primers according to the invention at RT of the solvent freed, tend to result in the case of PE improved adhesion properties the printing ink on the respective primer. Due to the forced drying at 100 ° C of the respective primer on the other hand are very good adhesion properties the printing ink found on the pretreated PE panels. in the Case of PP, liability is excellent, regardless of the temperature during evaporation of the solvents.

Also Here, the examples P4 to P6 show no significant compared to P1 Differences. Therefore, the influence of the solvent used is (Component C)) low.

Primer P1 was applied to Treofan NNA 40 (PP film) as described above. However, the ink was applied only 3 or 6 months after application of the primer. The investigation of the adhesion properties shows no differences in comparison to the investigations after direct application of the printing ink. It has therefore been proven that the adhesion-improving effect remains constant over a long period of time (see Table 6). Table 6. Results of the adhesion tests (wrinkle test, Tesatest) of the printing ink on the primer P1 on Treofan NNA 40 after 2 min and after 3 and 6 months of application of the primer sample Drying conditions of the primer crumple test tesa test 5 min 1 h 24 hours P1 2 min RT 1 1-2 1 1 3 months RT 0 1 1 1 6 months RT 0 1 1 1

Claims (43)

Non-reactive compositions that are not organic Contain bound chlorine, essentially containing A) 1 up to 98% by weight of at least one non-reactive poly-α-olefin, which contains no organically bound chlorine and a melting enthalpy in the range of 0 to 80 J / g and B) 1 to 98% by weight at least one ketone, ketone / aldehyde and / or urea / aldehyde resin and / or its hydrogenated secondary product and C) 1 to 98 wt .-% of at least one solvent and possibly D) up to 97% by weight of at least one auxiliary or aggregate, where the sum of the weights of the Components A) to D) is 100 wt .-%. Non-reactive compositions after at least one of the preceding claims, characterized in that as component A) non-reactive polyolefins used, which are soluble or swellable in organic solvents. Non-reactive compositions after at least one of the preceding claims, characterized in that as component A) atactic polypropylene and / or polybutene (1). Non-reactive compositions after at least one of the preceding claims, thereby in that as component A) unreactive poly-α-olefins are used, which essentially contain a) 0.5 to 100 wt .-%, preferably 1 to 99 wt .-%, particularly preferably 10 bis 98 wt .-% of one or more α-olefins with 4 to 20 carbon atoms, b) 1 to 99.5 wt .-%, preferably 1 to 99 wt .-%, particularly preferably 2 to 90 wt .-% propene and c) 0 to 50 wt .-%, preferably 0 to 20 wt .-% ethene. Non-reactive compositions after at least one of the preceding claims, thereby in that as component A) unreactive poly-α-olefins to be used, characterized by • a weight average molecular weight from 2,000 to 500,000 g / mol, preferably from 5,000 to 300,000 g / mol, more preferably from 7 500 to 200 000 g / mol, • a polydispersity PD of 2.0 to 60, preferably 2.5 to 40, particularly preferably 2.5 to 30, • a glass transition temperature Tg of -80 up to 0 ° C, preferably -60 up to 0 ° C, particularly preferred -55 to -10 ° C, • a melting enthalpy in the range of 0 to 80 J / g, preferably in the range of 1 to 70 J / g, more preferably in the range of 1 to 60 J / g as well as • a substantial one solubility and / or swellability in nonpolar solvents. Non-reactive compositions after at least one of the preceding claims, characterized in that as α-olefins with 4 to 20 carbon atoms of component A) 1-butene, 1-pentene, 1-hexene, 1-octene, 1-decene, 1-dodecene, 1-octadecene, 3-methyl-1-butene, a methylpentene such. For example, 4-methyl-1-pentene, a methylhexene or a Methylhepten be used alone or in mixture. Non-reactive compositions after at least one of the preceding claims, characterized in that as component A) at least one not reactive poly-α-olefin is used in amounts of 1 to 98 wt .-%, preferably from 1 to 49 wt .-%, particularly preferably 1 to 40 wt .-%. Non-reactive compositions after at least one of the preceding claims, characterized in that for the preparation of the ketone resins and / or Ketone-aldehyde resins (component B)) C-H-acid ketones can be used. Non-reactive compositions after at least one of the preceding claims, characterized in that for the preparation of the ketone resins and / or Ketone-aldehyde resins (component B)) ketones selected from acetone, acetophenone, Methyl ethyl ketone, tert-butyl methyl ketone, heptanone-2, pentanone-3, methyl isobutyl ketone, Cyclopentanone, cyclododecanone, mixtures of 2,2,4- and 2,4,4-trimethylcyclopentanone, Cycloheptanone, cyclooctanone, cyclohexanone, 4-tert-amylcyclohexanone, 2-sec-butylcyclohexanone, 2-tert-butylcyclohexanone, 4-tert-butylcyclohexanone, 2-methylcyclohexanone, 3,3,5-trimethylcyclohexanone as starting bonds used alone or in mixtures. Non-reactive compositions after at least one of the preceding claims, characterized in that for the preparation of the ketone-aldehyde resins (Component B)) acetophenone, cyclohexanone, 4-tert-butylcyclohexanone, 3,3,5-trimethylcyclohexanone and heptanone alone or in admixture be used. Non-reactive compositions after at least one of the preceding claims, characterized in that for the preparation of the ketone resins (component B)) cyclohexanone is used. Non-reactive compositions after at least one of the preceding claims, characterized in that for the preparation of the ketone-aldehyde resins (Component B)) aldehydes are used. Non-reactive compositions after at least one of the preceding claims, characterized in that for the preparation of the ketone-aldehyde resins (Component B)) formaldehyde, acetaldehyde, n-butyraldehyde and / or iso-butyraldehyde, valeric aldehyde, dodecanal alone or in mixtures be used. Non-reactive compositions after at least one of the preceding claims, characterized in that as an aldehyde component for the preparation the ketone-aldehyde resins (component B)) formaldehyde and / or para-formaldehyde and / or trioxane is used. Non-reactive compositions after at least one of the preceding claims, characterized in that as component B) resins of acetophenone, Cyclohexanone, 4-tert-butylcyclohexanone, 3,3,5-trimethylcyclohexanone, Heptanone alone or in mixture and formaldehyde. Non-reactive compositions after at least one of the preceding claims, characterized in that as component B) resins according to claims 8 to 15, which were hydrogenated after preparation, can be used. Non-reactive compositions after the previous one Claim, characterized in that hydrogenated as component B) Secondary products of the resins consisting of acetophenone, cyclohexanone, 4-tert-butylcyclohexanone, 3,3,5-trimethylcyclohexanone, heptanone be used alone or in mixture and formaldehyde. Non-reactive compositions according to at least one of the preceding claims, characterized in that as component B) urea-aldehyde resins, prepared using a urea of the general formula (i)

in which X is oxygen or sulfur, A is an alkylene radical and n is 0 to 3, with 1.9 (n + 1) to 2.2 (n + 1) mol of an aldehyde of the general formula (ii)

in which R ₁ and R _{2 are} hydrocarbon radicals each having up to 20 carbon atoms and / or formaldehyde used. Non-reactive compositions after at least one of the preceding claims, characterized in that as component B) urea-aldehyde resins prepared using urea, thiourea, methylene diurea, Ethylene diurea, tetramethylene diurea and / or hexamethylene diurea or mixtures thereof are used. Non-reactive compositions after at least one of the preceding claims, characterized in that as component B) urea-aldehyde resins prepared using isobutyraldehyde, formaldehyde, 2-methylpentanal, 2-ethylhexanal and 2-phenylpropanal or mixtures thereof used become. Non-reactive compositions after at least one of the preceding claims, characterized in that as component B) urea-aldehyde resins manufactured using urea, isobutyraldehyde and Formaldehyde be used. Non-reactive compositions according to at least one of the preceding claims, characterized in that at least one ketone, ketone / aldehyde, urea / aldehyde resin and / or its hydrogenated secondary product is used as component B), characterized by • a hydroxyl value between 0 and 450 mg KOH / g, preferably between 0 and 375 mg KOH / g, more preferably between 0 and 350 mg KOH / g, Gardner color number (50% by weight in ethyl acetate) between 0 and 5, preferably between 0 and 3.0, more preferably between 0 and 2.0, Gardner color number (50% by weight in ethyl acetate) after thermal loading of the resin (24 h, 150 ° C) between 0 and 10.0, preferably between 0 and 7.5, particularly preferably between 0 and 5.0, • a number average molecular weight Mn of 300 to 10,000 g / mol , preferably from 400 to 5000 g / mol, more preferably from 400 to 3000 g / mol, • a polydispersity (Mw / Mn) between 1.25 and 4.0, particularly preferably between 1.3 and 3.5, A melting point / range between 20 and 180 ° C, preferably between 30 and 140 ° C, more preferably between 40 and 130 ° C and a solubility in non-polar, organic solvents. Non-reactive compositions after at least one of the preceding claims, characterized in that as component B) at least one ketone, Ketone / aldehyde, urea / aldehyde resin and / or its hydrogenated Subsequent product is used, in amounts of 1 to 98 wt .-%, preferably 1 to 49 wt .-%, particularly preferably 1 to 40 wt .-%. Non-reactive compositions according to any one of previous claims, characterized in that organic solvents are used as component C) be used. Non-reactive compositions according to any one of previous claims, characterized in that aromatic, aliphatic and / or cycloaliphatic solvents selected from xylenes, toluene, benzene, cresols, naphthalene, tetrahydronaphthalene, Decahydronaphthalene, hexane, heptane, (methyl) cyclohexane, crystal oils, specialty and white spirits, turpentine, paraffins alone or in mixture be used as component C). Non-reactive compositions after at least one of the preceding claims, characterized in that the component C) in amounts of 1 to 98 wt .-%, preferably from 2 to 98 wt .-%, particularly preferably 20 to 98 wt .-% is contained in the composition. Non-reactive compositions according to any one of previous claims, characterized in that as component D) auxiliaries and additives be used. Non-reactive compositions according to any one of previous claims, characterized in that as component D) auxiliaries and additives, selected from inhibitors, other organic solvents, water, surface-active Substances, defoamers, ventilators, Slip and leveling agents, substrate wetting agents, antiblocking agents, Oxygen and / or Radical scavengers, Catalysts, light stabilizers, color whiteners, photosensitizers and initiators, additives for influencing rheological properties (Thixotropic and / or thickening agents), skin preventatives, Antistatic agents, wetting and dispersing agents, crosslinking agents (blocked or unblocked (poly) isocyanates), preservatives (fungicides and / or Biocides), thermoplastic additives, plasticizers, matting agents, Fire retardants, (internal) release agents, blowing agents, dyes, Pigments, fillers, Polyurethanes, polyacrylates, polyethers, polyesters, alkyd resins, Polyamides, casein, cellulose ethers, derivatives of cellulose, polyvinyl alcohols and derivatives of polyvinyl alcohols, polyvinyl acetates, polyvinylpyrolidones, Rubbers, natural resins, hydrocarbon resins (coumarone, indene, Cyclopentadiene resins), terpene resins, maleate resins, phenolic resins, Phenol / urea-aldehyde resins, aminoplasts (eg melamine, benzoguanamine resins), Epoxy acrylates, epoxy resins, silicic acid esters and alkali silicates (eg, water glass), silicone resins, fluorine-containing polymers alone or in mixture. Non-reactive compositions according to any one of previous claims, characterized by rapid drying and high blocking resistance. A process for the preparation of non-reactive compositions according to any one of the preceding claims, comprising substantially A) 1 to 98 wt .-% of at least one non-reactive poly-α-olefin containing no organically bound chlorine and a melting enthalpy in the range of 0 to 80 J / g and B) 1 to 98 wt .-% of at least one ketone, ketone / aldehyde, urea / aldehyde resin and / or its hydrogenated secondary product and C) 1 to 98 wt .-% of at least one solvent and optionally D) up to 97 wt .-% of at least one auxiliary or additive, wherein the sum of the weights of components A) to D) is 100 wt .-%, by intensive mixing and homogenization by stirring and / or dispersing the components A) to D) at temperatures of +20 to + 80 ° C, wherein the component C) is initially charged and the components A), B) and optionally D) are added. Use of non-reactive compositions according to at least one of the preceding claims as primer compositions to improve the adhesion to plastics. Use of non-reactive compositions according to at least one of the preceding claims as primer compositions to improve adhesion to untreated plastics. Use of the non-reactive compositions according to at least one of the preceding claims as primer compositions for improving the adhesion to unpretreated, low-energy plastics, having a surface tension below 40, preferably below 38, more preferably below 34 mN / m ² . Use of non-reactive compositions according to at least one of the preceding claims as primer compositions to improve adhesion to untreated, low-energy Plastics, selected of polypropylene (PP), modified polypropylene (e.g., polypropylene-ethylene copolymers (eg block copolymers or random copolymers)), polyethylene (PE), modified PE, polypropylene / ethylene-propylene-diene blends (PP / EPDM) with low EPDM content, PP / PE blends, rubbers, polyvinyl chloride as well as special polyesters. Use of non-reactive compositions according to at least one of the preceding claims as primer compositions to improve adhesion to glass. Use of non-reactive compositions according to one of the preceding claims as primer compositions, characterized in that optionally a pre-treatment directly after the production of the plastic at the plastic manufacturer (off-line) or directly in front of the application of the coating material (in-line) takes place. Use of non-reactive compositions according to one of the preceding claims as primer compositions, characterized in that the composition by means of (electrostatic) spraying, Spraying, spincoating, casting, dipping, drumming, flood, Rolling, wiping, washing, printing, rolling, brushing, extruding is applied to the plastic substrates. Use of non-reactive compositions according to one of the preceding claims as primer compositions, characterized in that the Primer layers subsequent adhesives, sealants and / or coating materials be applied. Use of non-reactive compositions according to one of the preceding claims as primer compositions, characterized in that the following Layer directly "wet-on-wet" on the primer layer is applied, or the primer first at room temperature or increased Temperature of the volatile Components is released and then the subsequent layer on the "dry" - that is, solvent-free - primer is applied. Use of non-reactive compositions according to one of the preceding claims as primer compositions, characterized in that the layer thickness of the primer layers after evaporation of the volatiles between 0.01 and 100 μm, preferably 0.1 and 30 μm, more preferably between 0.2 and 10 microns. Use of non-reactive compositions according to one of the preceding claims as primer compositions, characterized in that as subsequent Systems sealing, adhesive and coating materials are used selected from solvent-containing and / or aqueous Systems and / or solvent-free Systems (eg radiation-curable Adhesives, sealants, coating materials and / or powder coatings). Use of non-reactive compositions according to one of the preceding claims as primer compositions, characterized in that as subsequent Systems sealing, adhesive and coating materials are used selected from solvent-containing and / or aqueous Systems and / or solvent-free Systems (eg radiation-curable Adhesive, sealing, coating materials and / or powder coatings) such. As fillers, fillers, Base and / or topcoats, printing inks, ballpoint pen pastes, inks, Polishes, glazes, laminations, heat sealing lacquers, cosmetics and / or sealing and insulating materials as well as adhesives. objects prepared using non-reactive compositions at least one of the preceding claims.