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    • 专利摘要:
    1499173 Paint binders VIANOVA KUNSTHARZ AG 20 March 1975 [3 April 1974] 11713/75 Heading C3P Paint binders, especially forelectrodeposition, and which may be rendered water-soluble on neutralization with a base, are prepared by (1) reacting 70-90 wt. per cent of a diene polymer of M.W. 500-20,000 with 10-30 wt. per cent of an α,#-ethylenically unsaturated carboxylic acid component, (2) esterifying up to 70% of the carboxyl groups or latent carboxyl groups in the product with a monohydric alcohol, and (3) combining 80-98 wt. per cent of the partially esterified product with 2-20 wt. per cent of a resin-like polycarboxylic acid having an acid value of 150-350 mg KOH/g. which is an adduct of an α,#-ethylenically unsaturated carboxylic acid component with an unsaturated hydrocarbon resin or unsaturated fatty acid. In examples, liquid 1,4- or mixed 1,2/1,4-polybutadiene or a mixture of liquid 1,4-polybutadiene with an unsaturated hydrocarbon resin which is a cyclopentadiene/methylcyclopentadiene/isoprene copolymer are each reacted with maleic anhydride, then partially esterified with methanol, and then combined with a polycarboxylic acid component obtained by reacting maleic anhydride with linseed oil fatty acids, tall oil fatty acids or a liquid hydrocarbon resin which is a cyclopentadiene/methylcyclopentadiene/isoprene copolymer, followed by hydrolysis to produce free carboxyl groups. The final binder compositions are neutralized with ammonia.
    公开号:SU805950A3
    申请号:SU752119502
    申请日:1975-04-02
    公开日:1981-02-15
    发明作者:Дворак Герт
    申请人:Вианова Кунстхарц А.Г. (Фирма)；
    IPC主号:
    专利说明:

    (54) METHOD OF OBTAINING POLYMERIC BONDING
    The invention relates to the preparation of polymeric binders used as primer compositions, applied by electrostatic dipping and possessing an anti-corrosion one of your own, and can be used in the paint and varnish, woodworking industry. Methods are known for preparing a polymeric binder by treating polydienes with dL, P-unsaturated dicarboxylic acids in a mixture with natural oils or treating liquid polybutadiene with maleic anhydride in the presence of a copper catalyst fl and 2},. However, these products have a high degree of unsaturated bonds and when. technical application due to high activity to oxidation in air is not suitable. The closest to the present invention is a method for producing polymeric binders by treating polybuc. In chemical modification, the product is mixed with natural oils, etherified with a monohydric alcohol, and resinous polycarboxylic acids are obtained. However, a product of c. uneven distribution of acid groups, and hence the deterioration of the anti-corrosion properties of the coating based on such binders. The purpose of the invention is the corrosion resistance of binders. The goal is achieved in that the chemical modification is carried out by esterification with a monohydric alcohol, and then 80-95% by weight of the obtained product with 5-20% by weight of an adduct of maleic anhydride with unsaturated fatty acids of vegetable oils with an iodine number of 120-170 or with polycyclopentadiene with iodine number 190-250 with the content of macheic anhydride in the adduct 20-30 wt.%. To ensure the same degree of curing of the coating, the amount of polycarboxylic acid added to the diene polymer is less than when using chain-extending agents. As a result, it is possible to comparatively increase the content of unwashed dieno-polymerization in the composition of the binder, and, consequently, to improve against the corrosion properties of such coatings.
    The method for preparing the polymeric binder is carried out in several steps.
    1. A partially esterified product is obtained in a known manner by reacting polydiene with maleic anhydride at 150-250 ° C to: ensure complete binding of the anhydride and then reacting it with monohydric alcohols. In the reflux unit, the polydiene is low molecular, at room temperature mostly liquid Conjugated diolefin oligomers: butaLien -1.3; 2-methylbutadiene-1, 3-dimethylbutadiene-1, 3; cyclopentadiene, as well as their halogen derivatives, if necessary, used in the form of copolymers with styrene, ot-methylstyrene, vinyltoluene, vinyl acetate, (meth) acrylic esters (meth) acrylonitrile. These aligomers have a molecular weight of 1000-3000, a viscosity of 330 Pz when and contain mainly isolated double bonds, which can be partially hydrogenated; their iodine number is 300-500. Possible further modification of these diene polymerizates by graft polymerization with styrene, vinyltoluene d-methylstyrene, esters of (meth) acrylic acid, arylnitrile.
    Catalysts, preferably tertiary amines, can be USED to accelerate the esterification with a monohydric alcohol. At the same time, a maximum (70%) certification of cash or potentially cash is ensured. carboxyl groups, determining the acid number.
    Methanol, ethanol, n-propanol, isopropanol, n-butanol, isobutanol, secondary butanol, long-chain alkanols, as well as ethylene glycol hemi-ester, diethylene glycol, polyethylene glycols, propylene glycol, for example, simple monomethyl, simple monomer, can be used as simple monomer alcohols. ethylene glycol monobutyl ether, diethylene glycol monoethyl ether, propylene glycol monobutyl ether,
    2. The second component of the joint is separated from resinous polycarboxylic acids with an acid number of 150,350 mg KOH / G, o6pa3yeivffijx by reacting unsaturated fatty acids from Cfj - 0-2.4-maleic anhydride. As unsaturated fatty acid, fatty acid of linseed oil, tall oil, soybean and castor oil can be used.
    As unsaturated hydrocarbon resins, copolymers of cyclopentadiene, methylcyclopentadiene and isoprene with an average mineral weight of about 400 and 5 with an iodine number of 190-250 give good results. The adducts containing anhydrite groups are converted to a convenient form for processing with water and / or monohydric alcohols. For this partial etherification, all alcohols with the number of carbon atoms from 1 to 20 are suitable.
    3. A polymer binder is obtained by mixing 80.-98% by weight of an adduct obtained in 1 step with 2-20% by weight of resinous polycarboxylic acid, calculated on the dry matter of the resin.
    The polymer binder can be diluted with solvents to facilitate the work. The result is
    0 resin solutions with a binder content of 60-95%. Suitable solvents are alkanols, for example, methanol, ethanol, n-propanol, -isopropanol, n-butanol, secondary butanol,
    5 tertiary butanol, isobutanol, and
    glycol ethers, for example ethylene glycol monoethyl ether, monopropyl propylene glycol, diethyl diethylene glycol. Also suitable are ketones: methyl methyl ketone, methyl isobutyl ketone, 4-methoxy-4-methyl -2-pentanone, and diacetone alcohol.
    In order to be able to disperse (dissolve) the proposed carboxylic acid binding groups in water, they should be neutralized by at least 40%. Alkali metal hydroxides, for example KOH, can be used as neutralizers, mainly with nitrogen-containing compounds with basic nitrogen atoms, such as ammonia and aliphatic amines and gshkanolamine, for example, diethylamine, triethylamine and their
    5 homologs, diethanolamine, dimethylethanolamine, diinepropanolamine.
     Neutralized, at least partially, such binders are soluble in water or can be diluted with water, i.e. can
    It should be dispersed in water without storing the insoluble precipitate or the insoluble phase which builds into them during ordinary storage at the usual temperature. These aqueous solutions should not be MUST be completely transparent and may be slightly or moderately turbid. The binder solids content in these aqueous solutions is 30 to 40% in the ready-to-use binder.
    Such binders, pigmented without pigments, can be applied onto water-painted solutions in water, and it is advisable to apply them by electrostatic dipping, painting the part as an anode or painting it with a brush, dipping or spraying. Suggested svukidie. after drying, they give very corrosion-resistant coatings to a large extent, regardless of the quality of the preliminary treatment (preparation) of the painted surface. For industrial practice, this means eliminating (to a large extent) the complex operations of phosphating and chromatization of the surface surface required for enhancing the anti-corrosion properties of the coatings. Component 1A. 500 g of liquid .. yolibutadiene with a viscosity of 8 Pz with an iodine number of about 450 and a microstructure of about 70% 1,4-cis- / 28% 1,4-trans-, and 2% 1.2 1.5 g copper naphthenate with a metal content of 9% and 100 g of maleic anhydride is heated within 3 hours to 200 ° C in a three-necked flask with a working stirrer with reflux condenser and with a supply. Eynert6g6GGHGo 4-hour reaction at 200 ° C with the mixture is no longer free maleic anhydride is detected. After cooling the mixture to 90 seconds, s is added. 1 h 50 g of methanol The finished component has a dry matter content of 98% and an acid number at about 80 mg KOH / g. The viscosity of a solution of 58 g of component 1A and 42 g of ethylene glycol monoethyl ether is about 160 C (DIN, 53211 (20 ° C). - Component 2. A in a three-necked flask with an inert gas feed and reflux condenser is heated to 220 ° C 250 g of flax base oil and 100 g of maleic anhydride. After a 4-hour reaction, the free maleic anhydride is not detected in the mixture, the product is cooled to; diluted with 40 g of diacetone alcohol and hydrolyzed with water (30 g) acidic the number is after this 320 mg KOH / G, the dry matter content is ly equal to 86%.,; Component 1v. 400 g of liquid polybutadiene, as in component 1A, 1.5 copper naphthenate (metal content .9%) and 100..g of maleic anhydride are heated for 3,200 ° C a three-neck flask with a working mixer with a reflux condenser and an inert gas supply. After a 3-hour reaction, free maleic anhydride is not detected in the mixture. The mixture is cooled to 90-100 ° C. diluted with 50 g of diacetone alcohol and. etherify with a mixture of 35 g of methanol and 3 g of triethylamine. The acid number thereafter is 95-100 mg. . KOH / H. The dry matter content of the resin is 90%. : - ;. V. -:: ;; component 2B. In a three-necked flask with a stirrer, reflux condenser, and supply of inert gas, 250 g of tall oil fatty acid with resin content of 2% and 100 g of maleic anhydride are heated to 210 ° C for 3 hours. After 8 hours of reaction, no free maleic anhydride is detected. After lowering the temperature of cHCTehSi to 130 ° C, it is diluted with 40 g of diacetone alcohol, then further cooled to 90100 ° C and a mixture consisting of 30 g of water, 5 g of diacetone alcohol and 3 g of triethylamine is added. At the end of the hydrolysis, the acid number is 350 mg KOH / H. The dry matter content in the component is 86%. Component 1c. 425 g of liquid polybutadiene as in component 1A, 75 of an unsaturated hydrocarbon resin, which is a copolymer of cyclopentadiene, methylcyclopentadiene and isoprene with an average molecular weight of 4 r and iodine number of 190-200, G, g of copper naphthenate (metal content 9%) 100 g of maleic anhydride are heated for 3 hours to 200 ° C in a three-necked flask with a running stirrer under reflux and with an inert gas feed. After 3 hours, no free maleic anhydride was detected in the mixture. The mixture is cooled to 90-100 ° C and esterified with 100 g of ethylene glycol monoethyl ether to an acid number of 80 mg KOH / G. The dry matter content of the obtained resin was 98.5%. Component 2C. In a three-necked flask with a stirrer, a reflux condenser, and an inert gas supply, the ZOOH of a liquid hydrocarbon resin is heated for 3 hours to form a polymer of cyclopentadiene, methylcyclopentadiene and isoprene with an average molecular weight of about 400 and an iodine number of 190,200 100 g of maleic anhydride. After 7 hours of reaction, no free maleic anhydride is detected in the mixture. The system is cooled to 14, diluted with 60 g of diacetone alcohol, further cooled to 90 and rinsed with water. After 2 hours, the product is diluted with isopropanol to a dry matter content of 70%. Acid number 26D mg KOH / g. Component 1d. 500 g of liquid polybutadiene with a viscosity of 7 ° C at 25 ° C, an iodine number of about 400, and a microstructure of approximately 10% 1,4-g CZIS-, 45% -1,4-trans- and 45% 1,2- vinyl 1.5 g of copper naphthenate with a metal content of 9% and 100 g of maleic anhydride are heated for 3 hours to 20 ° C in a three-neck; a flask with a running stirrer with reverse cold. Dilkom and with inert supply
    gas. After 4 hours of reaction at 200 ° C, no free maleic anhydride is detected in the mixture. After cooling to 90 ° C, 4.50 g of methanol is added under reflux. The dry matter content in the finished component is 97%, and the acid number is about 80 mg KOH / g.
    Component 2D, 400 g of a commercial liquid hydrocarbon resin (defined as a copolymer of unsaturated C. and Su-hydrocarbons with a cyclopentadiene content of at least 40%, iodine number 230-250,, according to ASTM D 555) is treated with 100 g of maleic anhydride (20% of all load) at 200-210 ° C to complete the binding of maleic anhydride. After diluting with diacetone alcohol to a solids content, the 90% anhydride groups are split with water at 95 ° C and then the product is diluted with isopropylene with alcohol to a solids content of 70%. Acid number 220 mg KOH / g.
    Component 1B. 300 g of the liquid polybutadiene used in component 1A are treated with 100 g of maleic anhydride. The anhydride groups are then treated with methanol with their polyesterification and the product is diluted to 70% solid content with ethylene glycol monobutyl ether. The viscosity of a 50% strength solution in ethylene glycol monobutyl ether is 145 s (DKN 53211).
    Component 2 E. A mixture of 200 g of fatty alcohol of linseed oil and 125 g. Fatty acids (a mixture of fatty acids of dehydrated castor oil with an iodine number of 160-170) interacts with 100 g of maleic anhydride (23% of the whole load) to complete the reaction. Then the anhydride groups hydrolyze with water and the product is diluted to 80% ethylene glycol monoethyl ether. Acid number 245, mg KOH / g.
    Example. A mixture containing 595 g of component 1B and 33 g of component 2A is mixed with and diluted with igzopropanol (181 g) until a dry matter content of 70% is achieved. The ratio of these components is 95: 5 in terms of resin without solvent, the acid number of the system is 115 mg KOH / g .
    286 g of a 70% resin mixture are ground on a three-roll paintbrush with 32 g of titanium dioxide (rutile), 26 g of aluminum silicate, 2 g of pigment carbon black, 2 g of strontium chromate. The resulting 348 g of the paste is neutralized with the stirrer working with ammonia (0.2 mol) and slowly diluted with deieneated water to a dry matter content of 10% (based on the weight of the binder). This diluted lacquer solution has a pH of 7.05 and a conductivity of 3%.
    at 25 ° C. A 2.5 l metal container filled with this solution is included as a cathode in a direct current circuit. In the solution immerse the waste, a renal steel plate with a size of 200 include it as an anode. When a constant voltage of 180 V is applied, a dense, well-washed coating is applied to the plate. After drying the sample, a smooth coating of thick O is formed for 30 minutes.
    The results of tests on paints are given in the table.
    PRI mme R 2. 595 g component
    5 1B and 33 g of component 2B are mixed at 70 ° C and 181 g of isrpropanol are diluted to a dry matter content of 70%. The ratio of 95: 5. Further - as in example 1.
    1) Frost. A mixture of 627 g of component IA and 83 g of component 2B is diluted with isopropanol to a dry matter content of 70%. A component ratio of 90:10. Further, as in
    p-example
    The test results are shown in the table,
    EXAMPLE 4: 700 g of component 1C and 42.8 g of component 2B are mixed and the mixture is diluted with isopropanol (297 g to a dry matter content of 70%. The acid number of the system is 107 mg KOH / g, The viscosity of the solution from JR g of resin (70%) and 20 g of ethylene glycol is about 50 s (DIN 53211}. The ratio of components is 95: 5 based on solvent-free resins. Then, as in Example 1.
    The test results are given
    0 in the table.
    Example 5. 595 g of component 1B and 86 g of component .2С are mixed at 70 ° C and the mixture is diluted with isopropanol (l65 g) db of 70% dry matter content. Acid number 119.5 mg KOH / g , the ratio of components in a mixture is 90:10 in terms of resins that do not contain a solvent. Acid number SOO.g KON / g. dry matter content 70%. Further, as in Example 1.
    Example 657 g of component 1d and 83 g of component 2B are mixed at 70 ° C and the mixture is diluted with isopropanol to a dry matter content of 70%. The ratio of the components is 90:10. I
    The results of the tests are given
    in the table.
    PRI me R 7. 890 g of partial component 1B and 285 g of partial
    Component 2D is mixed at .70-8 ° C and diluted with isopropyl alcohol to 70% solids. The ratio of the partial components of the form of solid resin) 80:20, acid
    权利要求:
    Claims (3)
    [1]
    5 number 124.mg KOH / g. Technological properties of varnish are tested according to example 1. Example. 607 g of the partial component IE and 93 g of the partial component 2E are mixed at 70-Q09c and diluted with isopropyl alcohol to a solids content of 70%. The ratio of partial components 85; 15, the acid number of the product 150 mg KOH / Technological properties of varnish are tested according to example 1. 0 Comparative example. A binder according to example 1 is made, pigmented and diluted with water, for comparison with the examples of the proposed method, an elec- tron is produced. The trophoretic and bearing of the coating is not on a phosphated steel surface, but on defatted, non-phosphated steel of ordinary quality. NoKptrtuA test results are tabulated. 13 80595 Claim method for producing polymeric bonds by processing polybutadienes with a molecular weight of 1000-3000 and an iodine number of 300-500 15-25% by weight of maleic anhydride at 150-250 s, followed by chemical modification of the product obtained, in a fraction of By the fact that, in order to increase the corrosion resistance of the compounds, chemical modification is carried out by esterification with a monohydric alcohol, and then 80–95% by weight of the obtained product is mixed with 520% by weight of adduct of maleic anhydride 14 with unsaturated fatty acids vegetable oils with iodine number 120-170 or with polycyclopentine with an iodine number of 190-250 with maleic anhydride content in the adduct of 20-30 wt.%. Sources of information taken into account in the examination 1. US patent 3489704, cl. 260-23.7. publish 1970.
    [2]
    2. Patent of Germany No. 1219684, cl. 39 From 25/05, published. 1967.
    [3]
    3. Patent of Germany No. 2016223, cl. 39 in 15/40, published. 1972 (prototype).
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    引用文献:
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    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    AT278974A|AT328732B|1974-04-03|1974-04-03|PROCESS FOR THE PRODUCTION OF WATER-SOLUBLE BINDERS FOR ELECTRO-DIP PAINTING|
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