Process for coating an electrically conductive substrate and an aqueous coating composition based on a cationic binder

Abstract

A process is provided for coating an electrically conductive substrate with an aqueous coating composition containing a cationic binder wherein the binder is obtained by polymerization of 100 parts by weight of a specified monomer mixture in the presence of 1-45 parts by weight of a polymer built up to 70-100% by weight of 1,3-butadiene and 0-30% by weight of a copolymerizable monomer, having a number average molecular weight of 460-5400. The invention also pertains to the aqueous coating composition as such.

Description

The invention relates to a process for coating an electrically conductive substrate with an aqueous coating composition based on a cationic binder. The binder is obtained by polymerization of a monomer mixture in the presence of a polyethylenically unsaturated compound, the amino groups present in the binder being at least partially neutralized with an acid. The monomer mixture consists of (a) 1-30% by weight of a hydroxy(cyclo)alkyl(meth)acrylate of which the (cyclo)alkyl group contains 2-8 carbon atoms, (b) 4-45% by weight of an amino(meth)acrylate of the formula ##STR1## where at least one of the groups R.sub.1 is an organic group containing 1-12 carbon atoms and the other group R.sub.1 is an organic group containing 1-12 carbon atoms or a hydrogen atom, or the two groups R.sub.1, together with the nitrogen atom attached thereto, form a heterocyclic group, R.sub.2 is a hydrocarbon group containing 2-12 carbon atoms and R.sub.3 is a hydrogen atom or a methyl group, (c) 0-80% by weight of a monovinyl aromatic hydrocarbon containing 8-14 carbon atoms, (d) and 0-50% by weight of a different monoethylenically unsaturated monomer containing 2-20 carbon atoms. A process of the type indicated above is known from European Patent Application No. 104,683, the polyethylenically unsaturated compound proposed in it being a particular polyester. The resulting coating satisfactorily covers edges and displays good resistance to chemical attack and outdoor exposure. It has now been found, however, that the use of a different polyethylenically unsaturated compound results in a further improvement of the resistance to corrosion while the above properties are kept at the same level.

The process according to the invention is characterized in that the polyethylenically unsaturated compound is a polymer built up of 70-100% by weight of 1,3-butadiene and 0-30% by weight of a copolymerizable monomer and having a number average molecular weight of 460-5400. This polymer is present in an amount of 1-45 parts by weight per 100 parts by weight of the monomer mixture.

Examples of hydroxy(cyclo)-alkyl(meth)acrylates suitable for use in the monomer mixtures include hydroxyethyl acrylate, hydroxyethyl methacrylate, hydroxypropyl acrylate, hydroxypropyl methacrylate, hydroxybutyl acrylate, hydroxyhexyl acrylate, hydroxyoctyl acrylate and hydroxycyclohexyl acrylate. It is preferred that use should be made of hydroxyalkyl(meth)acrylates, more particularly hydroxyethyl acrylate and/or hydroxypropyl methacrylate. It is preferred that the monomer mixture should contain 5-24% by weight of hydroxy(cyclo)alkyl(meth)acrylate. As used herein, the term "hydroxy(cyclo)alkyl(meth)acrylates" refers to hydroxyalkyl acrylates, hydroxyalkyl methacrylates, hydroxycycloalkyl acrylates and/or hydroxycycloalkyl methacrylates.

Examples of amino(meth)acrylates suitable for use in the monomer mixture include methylaminoethyl(meth)acrylate, dimethylaminoethyl(meth)acrylate, diethylaminoethyl(meth)acrylate, propylaminoethyl(meth)acrylate, tert. butylaminoethyl(meth)acrylate, hexylaminobutyl(meth)acrylate, cyclohexylaminoethyl(meth)acrylate, dimethylcyclohexylaminoethyl(meth)acrylate, octylaminoethyl(meth)acrylate, dodecylaminoethyl(meth)acrylate, pyridylethyl(meth)acrylate and the chloride or sulphate of trimethylammoniumethyl(meth)acrylate. It is preferred that use should be made of a (di)alkylamino(meth)acrylate of which the alkyl group(s) has (have) 1-4 carbon atoms. More particularly, use is made of a .beta.-(di)alkylaminoethyl(meth)acrylate of which the alkyl group(s) has (have) 1-4 carbon atoms, for example: .beta.-dimethylaminoethyl(meth)acrylate and .beta.-di-ethylaminoethyl(meth)acrylate. It is preferred that the monomer mixture should contain 7-35% by weight, more particularly 7-28% by weight of amino(meth)acrylate.

The monomer mixture may contain as a third component a monovinyl aromatic hydrocarbon having 8-14, preferably 8-10 carbon atoms. Representative examples include styrene, .alpha.-methyl styrene, vinyl toluene and vinyl naphthalene. It is preferred that use should be made of styrene and/or vinyl toluene. It is preferred that the monomer mixture should contain 10-70% by weight of the monovinyl aromatic hydrocarbon.

Finally, the monomer mixture contains 0-50, preferably 0-45% by weight of some other monoethylenically unsaturated monomer having 2-20 carbon atoms, such as acrylic or methacrylic esters, for example: methyl methacrylate, ethyl acrylate, glycidyl methacrylate, butyl acrylate, 2-ethylhexyl acrylate, dodecyl acrylate and hexadecyl acrylate; nitriles, for example: acrylonitrile and methacrylonitrile; and compounds such as vinyl chloride, vinyl acetate and vinyl propionate; carboxylic acids such as acrylic acid, methacrylic acid, crotonic acid, itaconic acid and maleic acid may generally be applied in an amount not higher than about 1% by weight.

In addition to being built up of 1,3-butadiene the polymer to be used according to the invention may be formed of one or more comonomers, such as methacrylonitrile or styrene, more particularly acrylonitrile. For brevity, the polymer to be used according to the invention will be referred to here as butadiene polymer. It is preferred that the butadiene polymer should be built up of 80-100% by weight of 1,3-butadiene and 0-20% by weight of acrylonitrile.

Depending on the preparation procedure adopted, the butadiene polymer may also contain endgroups such as hydroxyl endgroups or carboxyl endgroups. The butadiene polymer may be built up in accordance with a 1,2-configuration, a cis-1,4-configuration or a trans-1,4-configuration; also applicable are mixtures of butadiene polymers of different configurations. Examples of representative butadiene polymers include the homopolymer of 1,3-butadiene having a 1,2-configuration of 50% and a 1,4-configuration of 50%; the homopolymer of 1,3-butadiene having a 1,4-configuration of more than 99%; the homopolymer of 1,3-butadiene having a 1,2-configuration of 88% and a trans-1,4-configuration of 12% and containing hydroxyl endgroups or carboxyl endgroups; and the copolymer of 1,3-butadiene containing 16% by weight of acrylonitrile and having a 1,2-configuration of 3.8%. The number average molecular weight of the butadiene polymer is preferably 900-3500. The preparation of the applicable butadiene polymers is totally known to the man skilled in the art and need not be further described here. It is preferred that the binder should be obtained by polymerization of 2-15 parts by weight of the butadiene polymer per 100 parts by weight of the monomer mixture.

Polymerization of the monomer mixture in the presence of the butadiene polymer may be carried out by methods known in themselves, use being made of a free radical initiator in an organic solvent at a temperature generally in the range of 10.degree. to 130.degree. C., use being made of ultraviolet radiation, if desired. For instance, polymerization may take place with continuous addition of a mixture of the monomers and initiator to a solution of the butadiene polymer and the monomer composition that is chosen may be constant or variable.

Examples of suitable solvents include polar solvents such as ketones, for instance: methylethyl ketone; alcohols, for instance: the ethyl ether or the butyl ether of ethylene glycol; and the ethyl ether of ethylene glycol acette. Generally, use is made of initiators which have such a half-life period at the chosen polymerization temperature that throughout the polymerization reaction a certain amount of initiator is present. Preferably, the polymerization is continued up to a conversion of the monomer mixture of at least 95%, more particularly 98-100%.

Examples of suitable radical initiators include 2.2'-azo-bis-isobutyronitrile, benzoyl peroxide, tert. butyl peroctoate and methylethyl ketone peroxide. The initiator is usually employed in an amount of 0.2-8, preferably 1-7% by weight, based on the weight of the monomer mixture. Optionally, the initiator may be added to the polymerization mixture batchwise.

For the resulting polymerization product to be made cationic and water-soluble, the amino groups present should at least partially be neutralized. This is generally done in a known manner and with the aid of an inorganic or organic acid. Examples of suitable acids include boric acid, phosphoric acid, sulphuric acid, sulphurous acid, hydrochloric acid, formic acid, acetic acid, propionic acid, glycolic acid, thioglycolic acid, diglycolic acid, lactic acid, thiopropionic acid, tartaric acid, malic acid or citric acid. Generally, use is made of mixtures of acids. It is preferred that use should be made of lactic acid. Neutralization may be carried out stepwise, if desired. It is preferred that 30-100% of the available amino groups of the binder should be neutralized. The pH of the composition is generally in the range of 3-7, preferably 4-5.

The preparation of the aqueous coating composition is effected in a simple manner, for instance by adding deionized water to the at least partly neutralized binder to a concentration level of about 30-50% by weight. Subsequently, the resulting solution is diluted with water to a commonly used concentration of 1-35% by weight, preferably 5-20% by weight.

The aqueous coating composition further contains a curing agent for the hydroxyl groups-containing polymerization product. Representative curing agents include blocked polyisocyanates. Examples of suitable polyisocyanates include aliphatic, cycloaliphatic or aromatic diisocyanates such as trimethylene diisocyanate, tetramethylene diisocyanate, hexamethylene diisocyanate, trimethyl hexamethylene diisocyanate, 1,2-propylene diisocyanate, 2,3-butylene diisocyanate, .omega.,.omega.'-dipropylether diisocyanate, 1,2-cyclohexane diisocyanate, 1,4-cyclohexane diisocyanate, isophorone diisocyanate, dicyclohexylmethane-4,4'-diisocyanate, 3,3'-dimethyl-dicyclohexylmethane-4,4'-diisocyanate, xylylene diisocyanate, 1,5-dimethyl-2,4-bis(isocyanatomethyl)benzene, 1,5-dimethyl-2,4-bis(2-isocyanatoethyl)benzene, 1,3,5-triethyl-2,4-bis(isocyanatomethyl)benzene, 4,4'-diphenylmethane diisocyanate, 2,4-toluene diisocyanate, 2,6-toluene diisocyanate, naphthalene diisocyanate, dianisidine diisocyanate, 4,4'-diphenylether diisocyanate.

Also suitable for use are higher functional polyisocyanates such as the adduct of 3 molecules of hexamethylene diisocyanate and 1 molecule of water (available under the trademark Desmodur N of Bayer), the adduct of 1 molecule of trimethylol propane and 3 molecules of toluene diisocyanate (available under the trademark Desmodur L of Bayer) and the adduct of 1 molecule of trimethylol propane and 3 molecules of isophorone diisocyanate, and compounds such as 1,3,5-triisocyanatobenzene and 2,4,6-triisocyanatotoluene.

Examples of suitable, known blocking agents for the polyisocyanate include alcohols, lactams, hydroxamates and oximes. As examples of suitable alcohols, which may be aliphatic, cycloaliphatic or alkylaromatic, may be mentioned propanol, 1-butanol, 2-butanol, isobutanol and pentanols. Examples of suitable lactams include .epsilon.-caprolactam, butyrolactam and 2-pyrrolidone. As examples of suitable oximes may be mentioned ethylmethyl ketoxime. Preference is given to the use of blocked polyisocyanates as curing agent in cases where the aqueous coating composition is to be applied to the substrate cataphoretically. Other curing agents are, for instance, N-methylol and/or N-methylol ether groups-containing aminoplasts obtained by reacting an aldehyde, for example formaldehyde, with an amino or amido groups-containing compound such as melamine, urea, N,N'-ethylene urea, dicyandiamide and benzoguanamine; for the preparation of these compounds see, for instance, Houben-Weyl, Methoden der organische Chemie, Volume 14/2, pp. 319-371 (1963). It is preferred that the afore-described compounds should entirely or partly be etherified with alcohols having 1 to 6 carbon atoms, for example with methanol, ethanol, n-propanol, isopropanol, n-butanol, isobutanol, amyl alcohol, hexanol or mixtures of the above-envisaged alcohols. Especially, use can be made of a methylol melamine having 4 to 6 methylol groups per melamine molecule, at least 3 methylol groups being etherified with methanol, ethanol, propanol or butanol. More particularly, use can be made of a hexaalkoxymethyl melamine, with the alkoxy group having 1 to 4 carbon atoms.

The aqueous coating composition may contain conventional adjuvants and additives, for instance: surface active compounds, anti-sag agents, dispersing agents, antioxidants, dispersion stabilizers, co-solvents, pigments and dyes. As examples of suitable pigments may be mentioned iron oxide, lead oxide, strontium chromate, carbon black, titanium dioxide, talc, silica, barium sulphate, cadmium yellow, cadmium red and phthalocyanine pigments.

As substrate there is used in the present process an electrically conductive substrate, which may for instance be of a pretreated or non-pretreated metal or alloy, such as iron, steel, zinc plated iron, copper, brass or aluminium, or an electrically conductive synthetic material or rubber.

The aqueous coating composition may be applied to an electrically conductive substrate for instance by brushing, spraying, dipping, electrostatic spraying, but preferably by cataphoresis. Cataphoresis may be carried out in the usual manner, for instance at a voltage of 50-500, preferably 100-350, and an initial current density of 0.1-40 A/m.sup.2. However, if desired, the aqueous coating composition may also be applied to any electrically non-conductive substrate.

After the coating has been applied to the substrate, it is baked at a temperature of, for instance, 90.degree.-250.degree. C., preferably 110.degree.-200.degree. C. The time required for baking depends on the backing temperature and generally varies between 5 and 45 minutes.

The invention also pertains to an aqueous coating composition based on a cationic binder. The binder is obtained by polymerization of a monomer mixture in the presence of a polyethylenically unsaturated compound, the amino groups present in the binder being at least partially neutralized with an acid. The monomer mixture consists of (a) 1-30% by weight of a hydroxy(cyclo)alkyl(meth)acrylate of which the (cyclo)alkyl group has 2-8 carbon atoms, (b) 4-45% by weight of an amino(meth)acrylate of the formula: ##STR2## wherein at least one of the groups R.sub.1 is an organic group having 1-12 carbon atoms and the other group R.sub.1 is an organic group having 1-12 carbon atoms or a hydrogen atom, or the two groups R.sub.1, together with the nitrogen atom attached thereto, form a heterocyclic group, R.sub.2 is a hydrocarbon group containing 2-12 carbon atoms and R.sub.3 is a hydrogen atom or a methyl group, (c) 0-80% by weight of a monovinyl aromatic hydrocarbon containing 8-14 carbon atoms, and (d) 0-50% by weight of a different monoethylenically unsaturated monomer containing 2-20 carbon atoms. The polyethylenically unsaturated compound is a polymer built up of 70-100% by weight of 1,3-butadiene and 0-30% by weight of a copolymerizable monomer and having a number average molecular weight of 460-5400 and which polymer is present in an amount of 1-45 parts by weight per 100 parts by weight of the monomer mixture.

The invention will be further described in, but not limited by, the following examples. Unless otherwise indicated, all parts and percentages are by weight. The cured coatings obtained according to the Examples were tested for hardness in conformity with NF T No. 30-016, for adhesion in accordance with DIN No. 53151, for impact resistance (back surface) in accordance with NF T No. 30-039 (drop height in cm of a mass of 1 kg until there is just not yet any crack formation in the coating) and for resistance to corrosion in an exposure for 400 hours to a salt spray in conformity with ASTM-B-117-64 (the results are expressed as C.sub.x YA.sub.z, where x and z denote the degree of rust formation in mm, respectively on either side of the scratch and on the edge of the panel, and the value y=10 means that there was no blistering). The edge covering was assessed by microscope. The thickness of the coating was measured in the cured state. The Gardner Holdt viscosity was measured at a temperature of 25.degree. C.

EXAMPLE 1

In a reactor equipped with a stirrer and a reflux condenser, 3.0 parts of a copolymer built up of 84% of 1,3-butadiene and 16% of acrylonitrile and having a 1,2-configuration of 3.8%, were mixed with 63.5 parts of monobutyl ether of ethylene glycol and the resulting mixture was heated to a temperature of 100.degree. C. Subsequently, a mixture of 53.3 parts of styrene, 17.9 parts of hydroxyethyl acrylate, 13.4 parts of methyl methacrylate, 10.7 parts of dimethylaminoethyl methacrylate and 1.95 parts of 2.2'-azo-bis-isobutyronitrile was introduced into the reactor in such a way that the temperature of the reactor contents did not rise to above 110.degree. C. After the monomer mixture had been added, the reactor contents were kept at a temperature of 100.degree. C. for 1 hour. Finally, a mixture of 0.96 parts of 2.2'-azo-bis-isobutyronitrile and 1.92 parts of monobutyl ether of ethylene glycol was added to the reactor contents in 2 equal portions, each of them over a period of 1 hour, in the process of which and for 2 more hours the reaction mixture was kept at a temperature of 100.degree. C. The resulting binder solution had a solids content of 59.0% and after dilution with monobutyl ether of ethylene glycol to a solids content of 50% it had a Gardner Holdt viscosity of Z3-Z5.

A coating composition was prepared by intermixing 64.0 parts of the aforedescribed binder solution, 17.0 parts of an 80%-solution of the adduct completely blocked with .epsilon.-caprolactam of 3 molecules of hexamethylene diisocyanate and 1 molecule of water in the methyl ether of propylene glycol acetate, 35.0 parts of rutile titanium dioxide, 6.0 parts of monobutyl ether of ethylene glycol, 1.5 parts of an 85%-aqueous solution of phosphoric acid and deionized water in an amount such that a composition having a solids content of 12.5% was obtained.

The aqueous coating composition was applied to a steel panel (Bonder 132) by cataphoretic deposition at a voltage of 250, a temperature of 26.degree. C. and an initial current density of 20 A/m.sup.2 to a coating thickness of 35-40 .mu.m and subsequently cured for 25 minutes at a temperature of 165.degree.-185.degree. C. The measured properties of the coating are given in the Table.

EXAMPLE 2

The procedure of Example 1 was repeated, except that use was made of 3.0 parts of the homopolymer of 1,3-butadiene having a 1,2-configuration of 88% and a trans-1,4-configuration of 12%, a number average molecular weight of 1350 and terminal carboxylic acid groups instead of the 3 parts of the butadiene-acrylonitrile copolymer, and of only 1.47 instead of 1.95 parts of 2.2'-azo-bis-isobutyronitrile in the monomer mixture. The measured properties of the coating are given in the Table.

EXAMPLE 3

In a reactor equipped with a stirrer and a reflux condenser 2.95 parts of a homopolymer built up of 1,3-butadiene having a 1,4-configuration of more than 99% and a number average molecular weight of 1500 were mixed with 63.7 parts of monobutylether of ethylene glycol and the resulting mixture was heated to a temperature of 100.degree. C. Subsequently, a mixture of 55.5 parts of styrene, 18.0 parts of hydroxyethyl acrylate, 11.4 parts of methyl methacrylate, 10.7 parts of dimethylaminoethyl methacrylate and 1.45 parts of 2.2'-azo-bis-isobutyronitrile was introduced into the reactor in such a way that the temperature of the reactor contents did not rise to above 110.degree. C. After the monomer mixture had been added, the reactor contents were kept at a temperature of 100.degree. C. for 1 hour. Finally, a mixture of 1 part of 2.2'-azo-bis-isobutyronitrile and 2.0 parts of monobutyl ether of ethylene glycol was added to the reactor contents in 3 equal portions, each of them over a period of 3/4 hours, in the process of which and for 2 more hours the temperature of the reaction mixture was kept at 100.degree. C. The resulting binder solution had a solids content of 59.2% and after dilution with monobutyl ether of ethylene glycol to a solids content of 50% it had a Gardner Holdt viscosity of Z2-Z4.

A coating composition was prepared by intermixing 64.0 parts of the aforedescribed binder solution, 17.0 parts of an 80%-solution of the adduct completely blocked with .epsilon.-caprolactam of 3 molecules of hexamethylene diisocyanate and 1 molecule of water in the methyl ether of propylene glycol acetate, 35.0 parts of rutile titanium dioxide, 6.0 parts of monobutyl ether of ethylene glycol, 1.5 parts of an 85%-aqueous solution of phosphoric acid and deionized water in an amount such that a composition having a solids content of 12.5% was obtained.

The aqueous coating composition was applied and cured in the same way as indicated in Example 1. The measured properties of the coating are indicated in the Table.

TABLE______________________________________ Examples 1 2 3______________________________________Hardness 290 300 310Adhesion Gt 0 Gt 0 Gt 0Impact resistance 35 <10 >50(back surface)Edge covering good good excellentSalt spray test C.sub.5 10 A.sub.3 C.sub.4 10 A.sub.2 C.sub.1 10 A.sub.0______________________________________

Claims

1. A process for coating a substrate, comprising applying to said substrate an aqueous coating composition based on a cationic binder obtained by polymerization of a monomer mixture in the presence of 1-45 parts by weight of a polyethylenically unsaturated compound per 100 parts by weight of the monomer mixture,

said monomer mixture consisting of (a) 1-30% by weight of a hydroxy(cyclo)alkyl(meth)acrylate of which the cyclo(alkyl) group contains 2-8 carbon atoms, (b) 4-45% by weight of an amino(meth)acrylate of the formula: ##STR3## where at least one of the groups R.sub.1 is a hydrocarbon group containing 1-12 carbon atoms and the other group R.sub.1 is a hydrocarbon group containing 1-12 carbon atoms or a hydrogen atom, or the two groups R.sub.1, together with the nitrogen atom attached thereto, form a heterocyclic group, R.sub.2 is a hydrocarbon group containing 2-12 carbon atoms and R.sub.3 is a hydrogen atom or a methyl group, (c) 0-80% by weight of a monovinyl aromatic hydrocarbon containing 8-14 carbon atoms, and (d) 0-50% by weight of a different monoethylenically unsaturated monomer containing 2-20 carbon atoms;

said polyethylenically unsaturated compound being a butadiene polymer built up of 70-100% by weight of 1,3-butadiene and 0-30% by weight of a copolymerizable monomer and having a number average molecular weight of 460-5400;

amino groups present in said binder being at least partially neutralized with an acid.

2. A process according to claim 1, wherein the hydroxy(cyclo)alkyl(meth)acrylate is at least one member selected from the group consisting of hydroxyethyl acrylate and hydroxypropyl methacrylate.

3. A process according to claim 1, wherein the monomer mixture contains 5-24% by weight of hydroxy(cyclo)alkyl(meth)acrylate.

4. A process according to claim 1, wherein the amino(meth)acrylate is a (di)alkylamino(meth)acrylate of which the alkyl group(s) has (have) 1-4 carbon atoms.

5. A process according to claim 1, wherein the amino(meth)acrylate is a .beta.-(di)alkylaminoethyl(meth)acrylate of which the alkyl group(s) has (have) 1-4 carbon atoms.

6. A process according to claim 1, wherein the monomer mixture contains 7-35% by weight of the amino(meth)acrylate.

7. A process according to claim 1, wherein the monomer mixture contains 7-28% by weight of the amino(meth)acrylate.

8. A process according to claim 1, wherein the monovinyl aromatic hydrocarbon has 8-10 carbon atoms.

9. A process according to claim 1, wherein the monovinyl aromatic hydrocarbon is at least one member selected from the group consisting of styrene and vinyl toluene.

10. A process according to claim 1, wherein the monomer mixture contains 10-70% by weight of the monovinyl aromatic hydrocarbon.

11. A process according to claim 1, wherein the monomer mixture contains 0-45% by weight of said different monoethylenically unsaturated monomer.

12. A process according to claim 1, wherein the butadiene polymer is built up of 80-100% by weight of 1,3-butadiene and 0-20% by weight of acrylonitrile.

13. A process according to claim 1, wherein the butadiene polymer has a number average molecular weight of 900-3500.

14. A process according to claim 1, wherein per 100 parts by weight of the monomer mixture 2-15 parts by weight of the butadiene polymer are polymerized.

15. A process according to claim 1, wherein the substrate is electrically conductive and the coating composition is applied to the substrate by cataphoretic deposition at a voltage of 50-500 and an initial current density of 0.1-40 A/m.sup.2.

16. A process according to claim 1, wherein the coating applied to the substrate is baked at a temperature of 90.degree.-250.degree. C.