Method of producing thermohardened binder for coating precipitated on cathode

专利摘要:
Cathodically depositable, aqueous coating compositions comprising the reaction product of (A) diene polymers containing free hydroxyl groups with a hydroxyl number of at least 40 mg KOH/g and an average maximum molecular weight of 4000; and (B) a compound having an average of from about 0.8 to 1.5 free isocyanate groups and at least one basic aliphatically bound nitrogen atom. Optionally, there can be included in the reaction product a compound having from about 0.8 to 1.5 free isocyanate groups and from 1 to 3 ethylenically unsaturated double bonds. The coating compositions cure at relatively low temperatures and relatively short curing times to provide films having excellent resistance to water, chemicals, and corrosion.
公开号:SU784790A3
申请号:SU772552300
申请日:1977-12-12
公开日:1980-11-30
发明作者:Пампухидис Георгиос；Даймер Вольфганг；Вердино Хайнер
申请人:Вианова Кунстхарц Аг (Фирма)；
IPC主号:

专利说明:

The invention relates to a method for producing a thermosetting binder for a coating deposited on a cathode. A method is known for producing a thermosetting binder for a coating deposited on a cathode by reacting a hydroxyl-containing compound, an iscyanate component and a compound containing a tertiary atom, in an inert solvent fl. However, the use of free amine in the preparation of coatings increases the toxicity of the process. The aim of the invention is to reduce the toxicity of the process. This goal is achieved by the fact that, as a hydroxyl-containing compound, 65-85 wt.% Of the proliferator with a hydroxyl number of 40-350 mg KOH / G are used, and the number-average molecular weight is not more than 5000, 5-30 weight is used as the isocyanate component. % in terms of hydroxyl-containing polyether of the reaction product of di- or polyisocyanate with a compound containing an active hydrogen atom and 1-8 olefins. As a compound containing a tertiary nitrogen atom, 15-35 wt.% of the reaction product of the di- or polyisocyanate, having 4,8-1,5, preferably 1, NCO-group, with amines of the general formula: b. where R is the residue of an alkanol or oxyphenyl; R and Rj are the residue of alkyl or cycloal: the process is carried out at 40-100, and the ten-thEn-enno mode is at 50-80 ° C. The reaction can take place, in the case of Necessity, in the presence of inert isocyanates with respect to isocyanates or canalizers. As the hydroxyl-containing polyether according to the invention, polyesters can be used, which are obtained by a known method of esterification of di- or polyols with monocarboxylic acids, dicarboxylic acids or polycarboxylic acids. As polyesters, according to the proposed method, resinous condensates with medium-molecular weight of maximum LOOO are used, which, along with free hydroxyl groups and groups with hydroxyl number of at least 40 mg KOH, contain at least two layers of ester groups in the molecule for more convenient further modification. Suitable di- or polyols are, for example, ethylene glycol, pr-nle, h-ol ol, b y t adiol, none and e or glycol, hexanediol or diols, which are derived from 4.4 -dioxydiphenyl - 2, 2-propane, t Kie as 1,1-isopropylidene-bis- (p phenyloxy) -, respectively, ethanol or 2-propanol, di-, and then glycerin, trimethylolpropane, trimethylolethane, pentaerythritol, castor oil, trioksoetnlizotsianurat. In addition, resinous polyols, such as styrene copolymers with allyl alcohol, which contain in: an average of 5 hydroxyl groups per molecule, or compounds with hidden hydroxyl groups, for example, simple and complex glyhydate esters, can also be used.
Suitable polycarboxylic acids are, for example, malonic acid, succinic acid, adipic acid, sebacic acid, malic acid anhydride, fumaric acid, O-phthalic anhydride, as well as isomeric or submidic acid, anhydride trimethyl phthalic acid, and acidic acid, succinic phthalic acid, acidic acid, anhydride, phthalic acid, anhydride, o-phthalic acid, and isome or phthalic acid, anhydride, trihydroxyphthalic acid, acidic acid, and isomeric or phthalic acid; fatty acids with non-cop: double bonds, etc.
Suitable monocarboxylic acids are, for example, caproic acid, nonanoic acid, isononanoic acid, decanoic acid, sorbic acid, benzoic acid, p-tert-butylbenzoic acid, as well as saturated and unsaturated fatty acids, which are contained in vegetable oils or animal oils. or fats.
As hydroxyl-containing resinous polycondensates according to the proposed method, one should also take into account the modification of polyethers, which, along with certain two ether groups, also contain urethane groups included in the remaining molecules. Also covered are such modifications which are obtained by polymerization of d-, 5-ethylenically unsaturated compounds with the aforementioned pelicone condensates. Such vinyl compounds or vinylidene compounds are, for example, acrylic ester, oxyalkyl acrylates, acrylamine, acrylonitrile, and also the corresponding methacrylates, styrene or vinyltoluene. The copolymerization can be carried out in a manner known in the presence of solvents and radical-forming initiators. The copolymerization can in particular be carried out to modify hydroxyl-containing resinous polycondensates that contain unsaturated fatty acids. Also, the concept of hydroxyl-containing resinous polycondensates encompasses such modifications that are obtained by the condensation of thermosetting phenolic resins with unsaturated fatty acid esters at elevated temperatures.
Further, suitable polyesters can be formed by condensation of substances with predominantly aliphatic bound carboxes: strong groups and amino alcohols, such as, for example, trioxymethylamine, and an oxazoline ring structure is formed with free hydroxyl groups.
The hydroxyl-containing polycondensate thus formed with a hydroxyl number of at least 40 mg KOH / G and a molecular weight of up to 5000 using the proposed method introduces a basic nitrogen atom. This is due to the transformation from compound m, which on average contains 0.8-1.5 isocyanate groups and at least one tertiary basic nitrogen atom per molecule. Preferably, these compounds contain about one isocyanate group per molecule.
Such compounds are prepared in a separate step of the process, and the diisocyanate or polyisocyanate is reacted with a stoichiometric deficiency of the amine of the general formula
X
TO.
where R is the aliphatic residue
alcohol or hydroxyphenyl; - alkyl or cycloalkyl residues.
Preferred are dialne, kilkoylolamine, such as dimethylethanolamine, diethylethanolamine, and that their higher homologues and isomers.
For example, aromatic isocyanates such as 2,4- or 2,6-toluene diisocyanate and their mixtures, 4,4-diphenylmethane diisocyanate or cycloaliphatic isocyanates such as isophorone diisocyanate, cyclohexane 1,4 diisocyanate, as well as aliphatic isocyanates, as well as aliphatic isocyanates, and also aliphatic isocyanates and aliphatic isocyanates. such as trimethylhexamethylene-1, b-diisocyanate; trihexmethylenetriisocyanate.
The interaction between the amine and the diisocyanate or the polyisocyanate occurs at 0-80 ° C, preferably at 20-50 ° C. The quantitative ratio of the reaction components is chosen such that the resulting compound contains 0.8-1.5, mostly one, isocyanate group. It is called hereinafter the main isocyanate forproduct.
To maintain thermal crosslinking of coatings deposited on the cathode, the reaction product is introduced into interaction with other compounds that contain, on average, 0.8-1.5 free isocyanate groups and from 1 to 3 olefinic unsaturated double bonds per molecule. These compounds are obtained in a separate stage from said diisocyanates or polyisocyanates with reaction components that, in addition to at least one hydrogen atom active towards isocyanates, contain from 1 to 3 more olefinic double bonds. Suitable {not asytsennymi compounds are, for example, hydroxyalkyl esters of acrylic acid or methacrylic acid trietilenglik olmonoakrilat-acrylate or methacrylate, trimetilolpropandimetakrilat LCID acrylate, adlilovyP alcohol tripropilenglikolmonoabietinat, oleyl alcohol or linolevyG: alcohol.
The reaction between the diisocyanate or the polyisocyanate and the active1.1 to the isocyanates by the olefinic saturated compound occurs in a particular case in inert to the isocyanates solvents at a temperature of from 10 to, mainly at 50-80 ° C, E if necessary in the presence of organic zinc compounds as catalysts, as long as the content of KSO-groups will be almost zero.
The amount of basic isocyanate pre-product is advantageously chosen in such a way that the basicity of the binding system after neutralization with acid gives sufficient solubility in water at pH values of 4–9, preferably 6–8. The conversion between the hydroxyl-containing polycondensate, the main isocyanate organic product and the olefinic / unsaturated isoatane can be carried out in any order, separately or together.
Following examples illustrate the invention, not organic. Getting preprodukty.
(A) Contents hydroxyl group polycondensate.
Component (A 1). 79 g of isonanoic acid, 89 g of tallic acid, 102 g of pentaerythritol, 45 g of trimethylolpropane and 120 g of isophthalic acid are heated under stirring to a three-neck flask with a separator, a reflux condenser and an inert gas. As soon as the acid number, the number padgchet to 12 mg KOlI / i is azeotroped with xylene. When the acid number drops below 3 mg KOH / g and the amount of reaction water reaches 42 g, they are circulating; agent in vacuum at low temperature. READY. KOMnoHetiT A 1 has a minimum solids content of 99%, a viscosity limit of 6 ml / g, measured in dimethylformamide at 20 ° C, and a hydroxyl number of 250 mg KOH / H.
Component (A 2). 300 g of wood oil is heated, as described, to 100 ° C. At this temperature, a mixture of 0.5 g of potassium hydroxide in 0.5 of monoethylene glycol is added. 48 g of pentaerythritol and 48 g of trimethylolpropane are then heated before and added. The temperature is immediately increased to 220 ° C and maintained at this value until a constant value of solubility in ethanol is reached. The temperature is lowered to 180 ° C and 113 g of a thermosetting phenolic resin, prepared from p-tert-butylphenol with formaldehyde, are started slowly in an alkaline solution. The reaction is complete when the viscosity of the solution of 72 g of component A 2 and 48 g of mono ethyl acetate, these. Glycol is 100 seconds.
0 (DJN 53 211), the hydroxyl number of the phenol-modified polyester is 280 mg KOH / g,
Component (A 3). 220 g of a copolymer of styrene and allyl alcohol with hydroxyles with acid 250 mg KOH / g is heated at 220 ° C with 140 g tall acid. As the acid number falls below 12 mg KOH / g, the reaction mass is supplemented by azeotropic distillation with xylene. When the acid number reaches 3 mg KOH / g, xylene is removed in vacuo at reduced temperature. The solids content in component A 3 is at least 99%,
5 g, croxyl number 80 mg KOH / g.
Component (A 4). 300 g of castor oil and 60 g of linseed oil are heated with stirring to 150 ° C. At this temperature and strong mixing, uniformly add a mixture of 80 g of vinyl toluene and 0.8 g of perexidi-tert-butyl. The temperature within an hour is raised to 20 ° C and maintained at this temperature until
5 until 90% of the added monomer reacts. In vacuum At lower temperatures, the excess vi is distilled off. and the temperature is reduced to 180 ° C. 117 g of trimethylolpropane, 1 g of calcium naphthenate (4%; and a solution of 0.5 g of potassium hydroxide in 0.5 g of mono-ethylene glycol are added immediately. After the addition, the temperature is raised to 240 ° C and the reaction is complete when the solubility is in n-butanol more
five
does not change. The polyether modified with an innative group has a hydroxyl number of 245 mg KOH / g.
Component (A 5). 485 g of dimethyltehthephthalate and 555 g of neopentyl glycol are placed in a round bottom flask with a stirrer, thermometer, vacuum cooler and water separator and heated to 170-200 C with stirring. At this temperature, the reaction is conducted until the theoretical amount of methanol is distilled off. . After that 645 g of adipic acid are added, and using xylene as; carrier continue the reaction at 170200 ° C to an acid number of 131 mg KOH / G. Then, at 150-160 ° C, add 415 g of trioxymethylaminomethane, heat to 170-190 0 and stir at this temperature until the acid number is less than 1 mg KOH / g The reaction product is diluted with ethyl glycol acetate to a solids content of 75%. The hydroxyl number is 224 mg KOH / g.
(c) Basic isocyanate pre-products.
component {in 1). 174 g of toluene diisocyanate {a mixture of 80% of the 2.4 and 20% of the 2.6 isomers) in a three-necked flask with a reflux condenser and inertial gas injection with an absolute absence of moisture and intensive cooling are uniformly reacted with 89 g of dimethyl ethanol amine diluted to 60 ethylene glycol monoethyl acetate. The reaction temperature does not exceed 25 ° C. The transformation is completed when the theoretical: isocyanate number reaches 16% or lower.
Component (2) .174 g of toluene diisocyanate (mixture of 80% of 2.4 and 20% of 2,6-isomers) are mixed in a three-neck flask with a reflux condenser and inert gas injected with absolute exclusion of moisture from 194 g of ethylene glycol monoethyl acetate. With vigorous stirring, 117 g of diethylethanolamine are added evenly over an hour at a temperature below. Isocyanate number of the final product is 14.4% ..
(c) Olefin-unsaturated isocyanate pre-products.
-Component (with 1). 168 g of hexamethylene diisocyanate are mixed in a three-necked flask with a condenser and in an inert gas, excluding moisture, with ethylene glycol 200 g of monoethyl acetate and heated to 60 ° C. At this temperature, a mixture of 130 g of hydroxyethylmethacrylate, stoubilized with hydroquinone, is added dropwise. The reaction ends after about 2 hours, when the isocyanate number reaches 14.1% or lower.
Component (C 2). 222 g of isophorone diisocyanate are mixed in a three-necked flask with a condenser and inert gas injected with exclusion of moisture from ethylene glycol monoethyl acetate 325 g and heated to 40 ° C. 265 g of linoleic alcohol are added evenly, and after the addition is completed, the temperature is raised to 90 ° C and held until the isocyanate number reaches 8.6.
Examples 1-7. In a reaction vessel equipped with a stirrer, a dropping funnel, a thermometer and a reflux condenser, hydroxyl-containing polycondensate (component A), if necessary in the presence of a solvent inert to the isocyanates, such as ethylene glycol monoethyl acetate, is added with the main isocyanate formate. (component B), which reacts completely at 40-100 ° C. Next, the reaction product is mixed, if necessary, with c1, n-olefinic unsaturated isocyanate pre-product (component C) and also dt reaction. at 40-100 ° C to an NCO value of 0.
The interaction of component A with component B and component C can also be carried out in one reaction stage at 40–100 –C, which does not significantly affect the results,
Further, these reaction products can be mixed with cross-linking resins, for example, urea, melamine, as well as phenol-formaldehyde resins, and they are conveniently converted by carefully conducting the reaction to a significant dilution with water,
The number of components, as well as the reaction conditions are presented in Table 1. Table
Continued table. one
All quantitative data refer to the solid resin content. The reactions of components B and C occur sequentially. The reactions of the components. B and C occur together BF: bis-phenol A - formaldehyde resin; MF: melamine - formaldehyde resin
FF: phenol-formaldehyde resins
Test the binder.
From the above binders, samples were mixed from 100 g of solid resin with an appropriate amount of acid and supplemented with deionized water until 1000, with stirring. From 10% solutions, coatings on steel plates were deposited by means of direct current, including the amount of acid, g per 100 g of solid resin;
Y is acetic acid, M is lactic acid;
measured in 10% aqueous solution;
tandem hardness (according to Koniq No. 53,157 / s);
Erichsen stretch test OIN h 53 156, mm;
the number of hours until the visible formation of corrosion or bubbles when kept in water at 40 ° C
The stability to the action of salts 117-64; 2 mm of corrosion in horizontal section after the specified number of hours. For these tests, pure, pre-rolled steel that has not been worked 5
allylamine groups.
as cathode. The deposition time in all cases was 60 s. The coatings were immediately washed with deionized water and hardened at elevated temperature. The average layer thickness of these flammable films was 13-17 microns.
Table 2 shows the results. Table 2 plates were coated with pigmented binder, which is per 100 weight.h,
. ,,, ..--- L
.., -,.
- 7 8 4 9 o
eleven
solid resin contained 20 parts by weight of mini silicate pigment and 2 parts by weight soot.

权利要求:
Claims (1)
[1]
1. US Patent No. 3883483, cl. 260-77.5, 03,06.75 (prototype).

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同族专利:

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公开号 | 公开日

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PL107822B1|1980-03-31|

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US4389509A|1983-06-21|

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YU294077A|1982-06-30|

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ES464960A1|1978-11-16|

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PL202880A1|1978-07-17|

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CA1094707A|1981-01-27|

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AT343770B|1978-06-12|

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BR7708226A|1978-09-05|

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ATA921076A|1977-10-15|

引用文献:

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AT356226B|1977-10-24|1980-04-10|Vianova Kunstharz Ag|METHOD FOR PRODUCING CATHODICALLY DEPOSIBLE BINDERS|AT366401B|1979-11-05|1982-04-13|Vianova Kunstharz Ag|METHOD FOR PRODUCING WATER-DETERMINATABLE BINDERS CARRYING OXAZOLIDING GROUPS|

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AU580856B2|1985-03-29|1989-02-02|Japan Synthetic Rubber Company Limited.|UV-ray curable resin composition and coated optical fiber|

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DE3829587A1|1988-09-01|1990-03-15|Bayer Ag|COATING AGENT, A PROCESS FOR THE PRODUCTION THEREOF, AND THE USE OF SELECTED TWO-COMPONENT POLYURETHANE SYSTEMS AS BINDER FOR SUCH COATING AGENTS|

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US6423425B1|1998-05-26|2002-07-23|Ppg Industries Ohio, Inc.|Article having a chip-resistant electrodeposited coating and a process for forming an electrodeposited coating|

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US6248225B1|1998-05-26|2001-06-19|Ppg Industries Ohio, Inc.|Process for forming a two-coat electrodeposited composite coating the composite coating and chip resistant electrodeposited coating composition|

法律状态:

优先权:

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申请号 | 申请日 | 专利标题

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AT921076A|AT343770B|1976-12-13|1976-12-13|PROCESS FOR THE PRODUCTION OF WARM-HARDENABLE BINDERS FOR CATHODICALLY SEPARABLE COATING COMPOUNDS|

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