CN1483772A - Low temp. solidifeed resin emulion used for cathode electrolytic coating - Google Patents

Low temp. solidifeed resin emulion used for cathode electrolytic coating Download PDF

Info

Publication number
CN1483772A
CN1483772A CNA031322557A CN03132255A CN1483772A CN 1483772 A CN1483772 A CN 1483772A CN A031322557 A CNA031322557 A CN A031322557A CN 03132255 A CN03132255 A CN 03132255A CN 1483772 A CN1483772 A CN 1483772A
Authority
CN
China
Prior art keywords
polyol
resin emulsion
flexible chain
weight
epoxy
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
CNA031322557A
Other languages
Chinese (zh)
Other versions
CN1235987C (en
Inventor
方基祥
缪蕾
陈卫东
熊挽志
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
CNOOC Changzhou EP Coating Co Ltd
CNOOC Changzhou Paint and Coatings Industry Research Institute Co Ltd
Original Assignee
CHANGZHOU INST OF PAINT CHEMICAL CHINESE CHEMICAL BUILDING CORP
JIANGSU HONGYE COATING SCIENCE AND TECHNOLOGY INDUSTRY Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by CHANGZHOU INST OF PAINT CHEMICAL CHINESE CHEMICAL BUILDING CORP, JIANGSU HONGYE COATING SCIENCE AND TECHNOLOGY INDUSTRY Co Ltd filed Critical CHANGZHOU INST OF PAINT CHEMICAL CHINESE CHEMICAL BUILDING CORP
Priority to CN 03132255 priority Critical patent/CN1235987C/en
Publication of CN1483772A publication Critical patent/CN1483772A/en
Application granted granted Critical
Publication of CN1235987C publication Critical patent/CN1235987C/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Paints Or Removers (AREA)
  • Epoxy Resins (AREA)

Abstract

The present invention relates to a low-temp. soldified resin emulsion for cathodic electrophoretic coating. It is made of 20-70% of modified epoxy resin, 5-50% of polyamine and 10-30% of closed polyisocyanate which can completely declosed at 120-140 deg.C, through the processes of chemical reaction, mixing, neutralizing with organic acid and dispersing in water, in which the modified epoxy resin is made up by using epoxy compound and polyhydroxylated compound and adopting epoxy resin synthesis method under the action of catalyst, its molecular weight is 300-3000, and the pure solid weight ratio of epoxy compound and polyhydroxylated compound is 5-8/2-5. The described epoxy compound is bisphenol A diglycidyl ether and glicidyl ether containing flexible chain or glycidyl ester, and the polyhydroxylated compound is bisphenol A and polyhydroxylated compound containing flexible chain.

Description

The cathode electrophoresis dope resin emulsion of low-temperature curing
Technical field
The present invention relates to a kind of cathode electrophoresis dope resin emulsion of low-temperature curing.
Background technology
In cathode electrophoresis dope, resin emulsion is main film forming matter, and it is determining the film performance of cathode electrophoresis dope, always is the emphasis that people research and develop.The epoxy type cathode electrophoresis dope is used widely because of it has excellent Corrosion Protection.As the resin emulsion of this class coating is that Resins, epoxy is carried out the amination open loop, add the dead front type polyisocyanates then and mix, in organic acid and after, in water, disperse to make.For guaranteeing good paint film property, solidification value is generally 160~200 ℃.Caused many practical problemss thus, caused the wasting of resources as the energy consumption height, cost improves; Can't be applicable to thermo-sensitive material; Paint film color is single, can't take into account the ornamental etc. of paint film.
Summary of the invention
The objective of the invention is to, a kind of cathode electrophoresis dope resin emulsion of low-temperature curing is provided,, can solidify and to give paint film ornamental at 120~140 ℃ with the paint film of the cathode electrophoresis dope of this resin emulsion preparation.
The technical scheme that realizes the object of the invention is: a kind of cathode electrophoresis dope resin emulsion of low-temperature curing, it is by modified epoxy 20~70%, polyamine 5~50% and can be at the blocked polyisocyanate 10~30% of 120~140 ℃ of complete deblockings, through chemical reaction and mixing, use again in the organic acid and after, dispersion is made in water, above percentage number average is with solid weight meter, wherein modified epoxy is epoxy compounds and polyol, under catalyst action, make with the Resins, epoxy synthetic method, molecular weight is 300~3000, its epoxy compounds is 5~8/2~5 with the pure solid weight ratio of polyol, described epoxy compounds is bisphenol A diglycidyl ether and glycidyl ether or the glycidyl ester that contains flexible chain, and described polyol is dihydroxyphenyl propane and the polyol that contains flexible chain.
Above-mentioned resin emulsion, as the glycidyl ether that contains flexible chain or the glycidyl ester of epoxy compounds, its weight is 5~50% of bisphenol A diglycidyl ether weight; As the polyol that contains flexible chain of polyol, its weight is 0~35% of dihydroxyphenyl propane weight.
Above-mentioned resin emulsion, the described glycidyl ether that contains flexible chain is neopentylglycol diglycidyl ether, butanediol diglycidyl ether, propylene glycol diglycidylether or ethylene glycol diglycidylether; The described glycidyl ester that contains flexible chain is tertiary carbonic acid glycidyl ester or Succinic Acid 2-glycidyl ester.
Above-mentioned resin emulsion, the described polyol that contains flexible chain are one or more in butyleneglycol, propylene glycol, hexylene glycol, a shrink ethylene glycol, butyl glycol ether, polypropylene glycol, polyoxyethylene glycol, polycaprolactone trivalent alcohol, the polycaprolactone dibasic alcohol.
Above-mentioned resin emulsion, described polyamine is the aliphatics amine, or the polycaprolactam polyamine class of modification, or both mixtures such as hexanediamine, diethylenetriamine, butanediamine, ketoimine, amino-polyether, polyamide resin, if select the modified polyamide resin, then the amine value is 50~500, is preferably 80~450.
Above-mentioned resin emulsion, described can be at the blocked polyisocyanate of 120~140 ℃ of complete deblockings, the encapsulant that is adopted is methyl ethyl ketoxime, methyl amylketone oxime, phenol, dimethyl pyrazole, diethyl pyrazoles, 1,2,4-triazole, diethyl malonate, acid amides alcohol, or their mixture.
Above-mentioned resin emulsion, described can be to adopt the Totally-enclosed-type of traditional method preparation or type semienclosed at the blocked polyisocyanate of 120~140 ℃ of complete deblockings, or both mixtures.Wherein used polyisocyanates can be an aliphatic polyisocyante, as trimethylene diisocyanate, tetramethylene diisocyanate, hexamethylene diisocyanate (HDI); Can be alicyclic polyisocyanates, as 1,3-pentamethylene vulcabond, 1,4-cyclohexyl diisocyanate, isophorone diisocyanate; Can be aromatic polyisocyanate, as tolylene diisocyanate (TDI), PPDI, to the phenylmethane vulcabond; Also can be the polymkeric substance of polyisocyanates, as the tripolymer of tolylene diisocyanate, the tripolymer of hexamethylene diisocyanate; Can also be polyisocyanate prepolymers, as the toluene diisocyanate prepolymer of TriMethylolPropane(TMP), the PPDI of polyoxyethylene glycol.
When the preparation modified epoxy, catalyst system therefor is benzyldimethylamine, 2-ethyl-4-methylimidazole or phosphines.Its consumption is 0.03~1% of a reactant gross weight, and temperature of reaction is 130~180 ℃, and the reaction times is 1~3 hour.
When preparation resin emulsion of the present invention, neutralization is lactic acid or acetic acid with organic acid.
Resin emulsion of the present invention has following characteristic index:
(1) solid content: 32~40%;
(2) tank liquor temperature: 25~35 ℃;
(3) construction voltage: 50~400V;
(4) film curing temperature: 120~140 ℃/30min of workpiece temperature.
Technique effect of the present invention: after adopting technical scheme of the present invention, since resin emulsion be adopt 120~140 ℃ fully the blocked polyisocyanate made of the encapsulant of deblocking make solidifying agent, and traditional pure ethers encapsulant such as ethylene glycol ethyl ether, butyl glycol ether etc., its complete deblocking temperature is at 170~180 ℃, though the complete deblocking temperature of hexanolactam is low slightly, but still need 160 ℃.Encapsulant of the present invention is getting final product complete deblocking below 140 ℃.Therefore, but with the formed paint film of cathode electrophoresis dope of such resin emulsion preparation 120~140 ℃ of completely solidified.In addition, for guaranteeing to have good levelling property at 120~140 ℃ of solidified paint films, determined modified epoxy in the technical solution of the present invention, by selected epoxy compounds and polyol and ratio thereof, control the molecular weight of modified epoxy, wherein in epoxy compounds and polyol, contain an amount of composition that contains flexible chain, make after the resin emulsion film forming, at the dry film that 120~140 ℃ of curing obtain, still have good ornamental.
Embodiment
Below in conjunction with embodiment the present invention is further described in detail, but is not limited to this.
Embodiment 1
One, preparation modified epoxy A
1, prescription sees Table 1
Table 1
Component Raw material Consumption (g)
Title Specification
Epoxy compounds GY 2600 (bisphenol A diglycidyl ether) Epoxy equivalent (weight) 187, Ciba company produces 140
Cardura E-10 (tertiary carbonic acid glycidyl ester is as the glycidyl ester that contains flexible chain) Epoxy equivalent (weight) 250, Shell company produces 13.4
Polyol Dihydroxyphenyl propane Commercially available, industrial goods 51
Polyethers 204 (polypropylene glycol is as the polyol that contains flexible chain) Hydroxyl equivalent 200, the DOW chemistry produces 15
Wherein: epoxy compounds/polyol weight ratio equals 6.97/3; The weight that contains the glycidyl ester of flexible chain is 9.5% of bisphenol A diglycidyl ether; The weight that contains the polyol of flexible chain is 29% of dihydroxyphenyl propane.
2, technological operation
In a four-hole boiling flask that is equipped with agitator, prolong, logical nitrogen pipe, thermometer, add 15g polyethers 204,140gGY2600 and 13.4gCardura E-10, also logical nitrogen in the presence of 0.2g benzyl dimethyl amine catalyst and 15g xylene solvent, be heated to 150 ℃, be incubated 2 hours, and then adding dihydroxyphenyl propane 51g, continuation was 150 ℃ of reactions 4 hours, cooling at last, add solvent ethylene glycol dibutyl ether 45g, propylene glycol phenylate 10g makes solid and is divided into 80% modified epoxy A, epoxy equivalent (weight) was 784 (not containing solvent), and is standby.
Two, preparation blocked polyisocyanate A-I
1, prescription sees Table 2
Table 2
Component Raw material Consumption (g)
Title Specification
Polyisocyanates HDT-90 (hexamethylene diisocyanate trimer) Rhodia produces (NCO content 19.8%) ????100
Encapsulant Methyl ethyl ketoxime Commercially available, industrial goods ????54
Catalyzer Dibutyl tin laurate Commercially available, industrial goods ????0.2
Solvent Hexone Commercially available, industrial goods ????10
Propylene glycol monomethyl ether Commercially available, industrial goods ????16
2, operating procedure
In a there-necked flask that is equipped with agitator, prolong, thermometer, add HDT-90 100g, hexone 10g, dibutyl tin laurate 0.2g, under 50 ℃, drip methyl ethyl ketoxime 54g then, dropwised in 2~3 hours, be warming up to 90 ℃ of insulations 2 hours with dropping funnel, cooling at last, add propylene glycol monomethyl ether 16g, make Totally-enclosed-type polyisocyanates A-I, discharging, standby, its solid is divided into 80%, and isocyanurate equivalent is 382.
Three, preparation resin emulsion A
1, prescription sees Table 3 tables 3
Component Raw material Consumption
Title Specification Weight (g) With the shared per-cent of solid weight meter (%)
Modified epoxy (A) The present embodiment self-control Solids constituent 80% epoxy equivalent (weight) is 784 ??200 ????68.6
Polyamine Diethanolamine Commercially available, industrial goods ??12 ????5.1
Hexanediamine Amine equivalent 58 is commercially available, industrial goods ??5.2 ????2.3
Blocked polyisocyanate (A-I) The present embodiment self-control Solids constituent 80% isocyanurate equivalent 382 ??70 ????24.0
2, operating procedure
Modified epoxy (A) 200g is joined 1000ml be equipped with in the there-necked flask of agitator, prolong, thermometer, be heated to 100 ℃, add diethanolamine 12g, 110 ℃ were reacted 2 hours, were cooled to 80 ℃ then, added hexanediamine 5.2g, 110 ℃ of reactions were cooled to 80 ℃ after 2 hours.Add blocked polyisocyanate (A-I) 70g, fully mixed 2 hours, add organic acid lactic acid 15g neutralization then at 80 ℃, continue to stir after 30 minutes, after adding deionized water 429g dispersion, form the cathode electrophoresis dope resin emulsion A of low-temperature curing, its solid is divided into 34.4%.
Four, resin emulsion A service check
Resin emulsion A mixed being made into varnish with deionized water by 4: 5 (weight ratio),,, under the construction voltage 200V, model is carried out electrophoretic painting 25 ℃ of tank liquor temperatures as the ability cathode electrophoresis tank liquor.The gained model was 120~140 ℃ of bakings 30 minutes after the application.Detecting model thickness by national standard method is 20~28 μ m; The visual inspection paint film, the outward appearance light is fine and smooth smooth, not xanthochromia; Film curing is (the two-way wiping of acetone is not seen loss of gloss 50 times) fully.
Embodiment 2
One, preparation modified epoxy B
1, prescription sees Table 4
Table 4
Component Raw material Consumption (g)
Title Specification
Epoxy compounds GY2600 (bisphenol A diglycidyl ether) Epoxy equivalent (weight) 187 Ciba companies produce ????150
Neopentylglycol diglycidyl ether (glycidyl ether that contains flexible chain) Epoxy equivalent (weight) 142 is commercially available, industrial goods ????10
Polyol Dihydroxyphenyl propane Commercially available, industrial goods ????50
Wherein: epoxy compounds/polyol weight ratio equals 6.40/2; The weight that contains the glycidyl ether of flexible chain is 6.67% of bisphenol A diglycidyl ether; Do not add the polyol that contains flexible chain in the polyol;
2, operating procedure
In a four-hole boiling flask that is equipped with agitator, prolong, logical nitrogen pipe, thermometer, add 10g neopentylglycol diglycidyl ether, 50g dihydroxyphenyl propane, 0.1g catalyzer benzyl dimethyl amine and 15g solvent xylene, under the situation of logical nitrogen, be heated to 150 ℃, be incubated 2 hours, be cooled to 100 ℃ then, add 150gGY2600, reacted 4 hours down at 150 ℃, cooling adds solvent propylene glycol monomethyl ether 37.5g, make the modified epoxy B of solids constituent 80%, epoxy equivalent (weight) was 484 (not containing solvent), and is standby.
Two, preparation blocked polyisocyanate B-I
1, prescription sees Table 5
Table 5
Component Raw material Consumption (g)
Title Specification
Polyisocyanates TDI (tolylene diisocyanate) Commercially available, industrial goods ???174
Encapsulant Methyl ethyl ketoxime Commercially available, industrial goods ???87
Catalyzer Dibutyl tin laurate Commercially available, industrial goods ???0.5
Solvent Hexone Commercially available, industrial goods ???29
2, operating procedure
In flask, add TDI 174g, hexone 29g, dibutyl tin laurate 0.5g drips methyl ethyl ketoxime 87g with dropping funnel under 30~40 ℃, dropwised in 3 hours, makes type semienclosed polyisocyanates B-I, and sealing is stored, and is standby.Solid is divided into 90%, and isocyanurate equivalent is 145.
Three, preparation blocked polyisocyanate B-II
1, prescription sees Table 6
Table 6
Component Raw material Consumption (g)
Title Specification
Polyisocyanates TDI (tolylene diisocyanate) Commercially available, industrial goods ??174.0
Encapsulant Methyl ethyl ketoxime Commercially available, industrial goods ??87.0
Glycol ether Commercially available, industrial goods ??42.4
PLACCEL-205 (poly-own interior pure dibasic alcohol) Japan Daicel company produces hydroxyl equivalent 265 ??53.0
Catalyzer Dibutyl tin laurate Commercially available, industrial goods ??0.3
Solvent Hexone Commercially available, industrial goods ??20.0
Propylene glycol monomethyl ether Commercially available, industrial goods ??69.0
2, operating procedure
In flask, add TDI 174g, hexone 20g, dibutyl tin laurate 0.3g drips methyl ethyl ketoxime 87g down at 36~40 ℃, be warming up to 80 ℃ of insulations 1 hour then, add glycol ether 42.4g then, react after 1 hour, add poly-own interior pure dibasic alcohol 53g again, continue reaction 2 hours, cooling adds propylene glycol monomethyl ether 69.0g, makes Totally-enclosed-type polyisocyanates B-II discharging, standby.Solid is divided into 80%, and isocyanurate equivalent is 445.
Four, preparation resin emulsion B
1, prescription sees Table 7
Table 7
Component Raw material Consumption
Title Specification Weight (g) With the shared per-cent of solid weight meter (%)
Modified epoxy (B) The present embodiment self-control Solids constituent 80% epoxy equivalent (weight) 484 ??200 ????50.5
Polyamine Diethanolamine Commercially available, industrial goods ??23.9 ????7.5
Polyetheramine JeffammeD-2000 HUNTSMAN company produces, amine equivalent 1000 ??76.1 ????24.0
Blocked polyisocyanate Present embodiment self-control B-I Solids constituent 90% (isocyanurate equivalent 145) ??10.0 ????2.8
Present embodiment self-control B-II Solids constituent 80% (isocyanurate equivalent 445) ??60.0 ????15.2
2, operating procedure
With above-mentioned modified epoxy (B) 200g, join 1000ml and be equipped with agitator, prolong, in the there-necked flask of thermometer, be heated to 100 ℃, add diethanolamine 23.9g, 110 ℃ were reacted 2 hours, be cooled to 90 ℃ and add polyetheramine JeffamineD-2000 76.1g, 80~90 ℃ of insulation reaction 3 hours add type semienclosed polyisocyanates B-I 10g, 75~80 ℃ of reactions 1 hour, add Totally-enclosed-type polyisocyanates B-II 60g again, thorough mixing adds lactic acid 20g neutralization after 1 hour, add deionized water 542g after 15 minutes, disperse the back to form the cathode electrophoresis dope resin emulsion B of low-temperature curing, its solid is divided into 34.8%.
Five, resin emulsion B service check
Press same procedure check among the embodiment 1, the gained result is with identical with resin emulsion A.
Resin emulsion of the present invention cooperates also with the pigment slurry that suits can make colored paint.The condition application of adopting the cathode electro-coating method to press embodiment 1, the gained paint film toasted 30 minutes down at 120~140 ℃, and paint film fully solidifies (the two-way wiping of acetone is not seen loss of gloss 50 times), and the outward appearance light is fine and smooth, not xanthochromia.

Claims (7)

1, a kind of cathode electrophoresis dope resin emulsion of low-temperature curing, it is characterized in that: it is by modified epoxy 20~70%, polyamine 5~50% and can be at the blocked polyisocyanate 10~30% of 120~140 ℃ of complete deblockings, through chemical reaction and mixing, use again in the organic acid and after, dispersion is made in water, above percentage number average is with solid weight meter, wherein modified epoxy is epoxy compounds and polyol, under catalyst action, make with the Resins, epoxy synthetic method, molecular weight is 300~3000, its epoxy compounds is 5~8/2~5 with the pure solid weight ratio of polyol, described epoxy compounds is bisphenol A diglycidyl ether and glycidyl ether or the glycidyl ester that contains flexible chain, and described polyol is dihydroxyphenyl propane and the polyol that contains flexible chain.
2, resin emulsion according to claim 1 is characterized in that: as the glycidyl ether that contains flexible chain or the glycidyl ester of epoxy compounds, its weight is 5~50% of bisphenol A diglycidyl ether weight; As the polyol that contains flexible chain of polyol, its weight is 0~35% of dihydroxyphenyl propane weight.
3, resin emulsion according to claim 1 and 2 is characterized in that: the described glycidyl ether that contains flexible chain is neopentylglycol diglycidyl ether, butanediol diglycidyl ether, propylene glycol diglycidylether or ethylene glycol diglycidylether; The described glycidyl ester that contains flexible chain is tertiary carbonic acid glycidyl ester or Succinic Acid 2-glycidyl ester.
4, resin emulsion according to claim 1 and 2, its feature also is: the described polyol that contains flexible chain is one or more in butyleneglycol, propylene glycol, hexylene glycol, a shrink ethylene glycol, butyl glycol ether, polypropylene glycol, polyoxyethylene glycol, polycaprolactone trivalent alcohol, the polycaprolactone dibasic alcohol.
5, resin emulsion according to claim 1 is characterized in that: described polyamine is the aliphatics amine, or the polycaprolactam polyamine class of modification, or both mixtures.
6, resin emulsion according to claim 1, it is characterized in that: described can be at the blocked polyisocyanate of 120~140 ℃ of complete deblockings, the encapsulant that is adopted is methyl ethyl ketoxime, methyl amylketone oxime, phenol, dimethyl pyrazole, diethyl pyrazoles, 1,2,4-triazole, diethyl malonate, acid amides alcohol, or their mixture.
7, according to claim 1 or 6 described resin emulsions, it is characterized in that: described can be the Totally-enclosed-types that adopt the traditional method preparation at the blocked polyisocyanate of 120~140 ℃ of complete deblockings, or type semienclosed, or both mixtures.
CN 03132255 2003-08-04 2003-08-04 Low temp. solidifeed resin emulion used for cathode electrolytic coating Expired - Fee Related CN1235987C (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 03132255 CN1235987C (en) 2003-08-04 2003-08-04 Low temp. solidifeed resin emulion used for cathode electrolytic coating

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 03132255 CN1235987C (en) 2003-08-04 2003-08-04 Low temp. solidifeed resin emulion used for cathode electrolytic coating

Publications (2)

Publication Number Publication Date
CN1483772A true CN1483772A (en) 2004-03-24
CN1235987C CN1235987C (en) 2006-01-11

Family

ID=34154066

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 03132255 Expired - Fee Related CN1235987C (en) 2003-08-04 2003-08-04 Low temp. solidifeed resin emulion used for cathode electrolytic coating

Country Status (1)

Country Link
CN (1) CN1235987C (en)

Cited By (19)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101362919B (en) * 2008-09-25 2010-12-08 江泽平 Single-component cationoid water-soluble epoxy-polyurethane anticorrosion primer system drying at 150 DEG C
CN101368057B (en) * 2008-09-25 2011-09-14 江泽平 High-performance 150 DEG C oven dry type bi-component epoxy-polyurethane cathode electrophoretic paint
CN103145951A (en) * 2013-03-20 2013-06-12 上海金力泰化工股份有限公司 Viscosity-reduction toughness-increasing and in-situ synthesizing method of low VOC (Volatile Organic Compound) cathode electrophoretic paint resin
CN103305110A (en) * 2013-06-24 2013-09-18 浩力森涂料(上海)有限公司 Low-temperature cured negative electrode electrophoretic paint and preparation method thereof
CN104900296A (en) * 2015-06-12 2015-09-09 江苏广信感光新材料股份有限公司 Conductive silver paste for membrane switch, and preparation method for conductive silver paste
CN105037686A (en) * 2015-08-14 2015-11-11 广东科富科技股份有限公司 Preparation method of epoxy cathodic electrophoretic coating anti-cratering resin
CN105907284A (en) * 2016-06-02 2016-08-31 广德县中银化工有限责任公司 Low temperature curable cathodic electrophoretic paint
CN105969057A (en) * 2016-06-02 2016-09-28 广德县中银化工有限责任公司 Low-temperature curing cathode electrophoretic paint and preparing process thereof
CN106047055A (en) * 2016-06-02 2016-10-26 广德县中银化工有限责任公司 Preparing technology for low-temperature setting cathode electrophoresis paint
CN106118410A (en) * 2016-06-22 2016-11-16 广德瑞邦涂料有限公司 A kind of cathode electrophoresis dope of environmental protection
CN106398469A (en) * 2016-08-31 2017-02-15 浩力森涂料(上海)有限公司 Microcapsule, self-healing electrophoretic coating containing microcapsule and preparation method of microcapsule
CN106715513A (en) * 2014-09-22 2017-05-24 荒川化学工业株式会社 Modified epoxy resin for coating material, and single component lacquer type coating material
CN107619576A (en) * 2017-08-11 2018-01-23 河北晨阳工贸集团有限公司 Self-emulsifying cation epoxy emulsion and preparation method thereof
CN109137047A (en) * 2018-09-06 2019-01-04 长春理工大学 A method of in metal surface, electroluminescent deposition prepares latex film
CN109251482A (en) * 2018-08-28 2019-01-22 广东科德环保科技股份有限公司 Modified epoxy and its preparation method and application, cathode electrophoresis dope and its preparation method and application
CN109627422A (en) * 2018-11-19 2019-04-16 万华化学集团股份有限公司 A kind of preparation method of diacetylmonoxime blocked polyisocyanates
CN110719941A (en) * 2017-05-12 2020-01-21 安格斯化学公司 Ether amine compositions and coatings
CN111234678A (en) * 2018-11-28 2020-06-05 立邦涂料(中国)有限公司 Tin-free environment-friendly low-temperature electrophoretic coating and preparation method thereof
US11426762B2 (en) 2015-12-31 2022-08-30 Henkel Ag & Co. Kgaa Low bake autodeposition coatings

Cited By (28)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101368057B (en) * 2008-09-25 2011-09-14 江泽平 High-performance 150 DEG C oven dry type bi-component epoxy-polyurethane cathode electrophoretic paint
CN101362919B (en) * 2008-09-25 2010-12-08 江泽平 Single-component cationoid water-soluble epoxy-polyurethane anticorrosion primer system drying at 150 DEG C
CN103145951A (en) * 2013-03-20 2013-06-12 上海金力泰化工股份有限公司 Viscosity-reduction toughness-increasing and in-situ synthesizing method of low VOC (Volatile Organic Compound) cathode electrophoretic paint resin
CN103145951B (en) * 2013-03-20 2016-06-15 上海金力泰化工股份有限公司 The viscosity reduction of low VOC cathode electrophoresis dope resin increases tough and in-situ synthetic method
CN103305110A (en) * 2013-06-24 2013-09-18 浩力森涂料(上海)有限公司 Low-temperature cured negative electrode electrophoretic paint and preparation method thereof
CN103305110B (en) * 2013-06-24 2016-03-02 浩力森涂料(上海)有限公司 A kind of low-temperature curing cathode electrophoresis coating and preparation method thereof
CN106715513A (en) * 2014-09-22 2017-05-24 荒川化学工业株式会社 Modified epoxy resin for coating material, and single component lacquer type coating material
CN106715513B (en) * 2014-09-22 2019-04-23 荒川化学工业株式会社 Coating modified epoxy and one pack system paint shaped coating
CN104900296A (en) * 2015-06-12 2015-09-09 江苏广信感光新材料股份有限公司 Conductive silver paste for membrane switch, and preparation method for conductive silver paste
CN105037686B (en) * 2015-08-14 2017-09-01 佛山科富科技有限公司 A kind of preparation of the anti-shrinkage cavity resin of Epoxy Cathodic Electrodeposition Coating
CN105037686A (en) * 2015-08-14 2015-11-11 广东科富科技股份有限公司 Preparation method of epoxy cathodic electrophoretic coating anti-cratering resin
US11426762B2 (en) 2015-12-31 2022-08-30 Henkel Ag & Co. Kgaa Low bake autodeposition coatings
CN106047055A (en) * 2016-06-02 2016-10-26 广德县中银化工有限责任公司 Preparing technology for low-temperature setting cathode electrophoresis paint
CN105969057A (en) * 2016-06-02 2016-09-28 广德县中银化工有限责任公司 Low-temperature curing cathode electrophoretic paint and preparing process thereof
CN105907284A (en) * 2016-06-02 2016-08-31 广德县中银化工有限责任公司 Low temperature curable cathodic electrophoretic paint
CN106118410A (en) * 2016-06-22 2016-11-16 广德瑞邦涂料有限公司 A kind of cathode electrophoresis dope of environmental protection
CN106398469A (en) * 2016-08-31 2017-02-15 浩力森涂料(上海)有限公司 Microcapsule, self-healing electrophoretic coating containing microcapsule and preparation method of microcapsule
US11466152B2 (en) 2017-05-12 2022-10-11 Angus Chemical Company Ether amine compositions and coatings
CN110719941A (en) * 2017-05-12 2020-01-21 安格斯化学公司 Ether amine compositions and coatings
CN107619576A (en) * 2017-08-11 2018-01-23 河北晨阳工贸集团有限公司 Self-emulsifying cation epoxy emulsion and preparation method thereof
CN109251482A (en) * 2018-08-28 2019-01-22 广东科德环保科技股份有限公司 Modified epoxy and its preparation method and application, cathode electrophoresis dope and its preparation method and application
CN109251482B (en) * 2018-08-28 2021-04-09 广东科德环保科技股份有限公司 Modified epoxy resin, preparation method and application thereof, cathode electrophoretic coating, preparation method and application thereof
CN109137047B (en) * 2018-09-06 2020-07-24 长春理工大学 Method for preparing latex film on metal surface by electro-deposition
CN109137047A (en) * 2018-09-06 2019-01-04 长春理工大学 A method of in metal surface, electroluminescent deposition prepares latex film
CN109627422B (en) * 2018-11-19 2021-04-20 万华化学集团股份有限公司 Preparation method of butanone oxime closed polyisocyanate
CN109627422A (en) * 2018-11-19 2019-04-16 万华化学集团股份有限公司 A kind of preparation method of diacetylmonoxime blocked polyisocyanates
CN111234678A (en) * 2018-11-28 2020-06-05 立邦涂料(中国)有限公司 Tin-free environment-friendly low-temperature electrophoretic coating and preparation method thereof
CN111234678B (en) * 2018-11-28 2023-07-28 立邦涂料(中国)有限公司 Tin-free environment-friendly low-temperature type electrophoretic paint and preparation method thereof

Also Published As

Publication number Publication date
CN1235987C (en) 2006-01-11

Similar Documents

Publication Publication Date Title
CN1235987C (en) Low temp. solidifeed resin emulion used for cathode electrolytic coating
JP5254121B2 (en) Polyisocyanurate composition, method for producing the same, and polyurethane resin
CN1329625A (en) Malonic acid ester/triazole mixed HDI trimer/formaldehyde stabilization
CN1878815A (en) Highly reactive polyurethane compositions containing uretdione groups
EP2185616A1 (en) Reactive isocyanate compositions
CN102892751B (en) The method of cyclic guanidine and the coating composition containing this cyclic guanidine is prepared by Dyhard RU 100
CN1472263A (en) Steel-structure anti-corrosion coating and preparing mehtod thereof
CN103626956B (en) A kind of modified polyisocyanate, water dispersible crosslinker and preparation method thereof
CN1105758C (en) Resin composition for cationic electrodeposition coating
US20020177674A1 (en) Resin composition for coating
CN1368525A (en) Amino-polyether modified epoxy and cationic cataphoresis paint composition containing the epoxy
CN1188443C (en) Polyurethane having hydroxy function of t-amino-formate bond
CN103342943B (en) Method for preparing high-charge-density cathode electrophoretic paint
CN1074027C (en) Preparation of resin emulsion for electrophoretic paint used on thick-film cathode
CN104774317B (en) A kind of preparation method of side chain alkyl polyurethane chain extender and products thereof
CN101522823A (en) Conductivity control agent for cationic electrodeposition coating material and method of regulating electric conductivity of cationic electrodeposition
CN1762987A (en) Biuretized polyisocyanates and blocked biuretized polyisocyanates
CN1927901A (en) High weatherability resin, preparation method thereof and coating composition containing the same
JP7236531B2 (en) Block isocyanate, method for producing multilayer film, and multilayer film
CN101595148B (en) A cathodic electrodeposition coating compositions having improved curing and anti-corrosion resistance
CN114262422A (en) Polyurea resin and preparation method and application thereof
WO2006002811A1 (en) Method for producing amino-functional polyurethane prepolymers
EP3805228A1 (en) A method for preparation of an isosorbide-based photocurable composition
AU689191B2 (en) Process for the preparation of a modified polymer for powder paints
CN1931888A (en) Radiation-curable polyurethane resin compositions with controlled structures

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
ASS Succession or assignment of patent right

Owner name: CNOOC CHANGZHOU PAINT + COATINGS INDUSTRY RESEARCH

Free format text: FORMER OWNER: CHANGZHOU INST OF PAINT CHEMICAL, CHINESE CHEMICAL BUILDING CORP.

Effective date: 20120910

Owner name: CNOOC CHANGZHOU EP COATING CO., LTD.

Free format text: FORMER OWNER: JIANGSU HONGYE COATING SCIENCE AND TECHNOLOGY INDUSTRY CO., LTD.

Effective date: 20120910

C41 Transfer of patent application or patent right or utility model
TR01 Transfer of patent right

Effective date of registration: 20120910

Address after: 213016 Changzhou Zhong Road, Jiangsu Province, No. 22 Longjiang Road

Patentee after: CNOOC CHANGZHOU EP COATING Co.,Ltd.

Patentee after: CNOOC CHANGZHOU PAINT & COATINGS INDUSTRY Research Institute

Address before: 213016, Jiangsu, Changzhou Province West Ring Road North intersection

Patentee before: JIANGSU HONGYE PAINT SCI & TEC

Patentee before: CNOOC Changzhou Paint and Coatings Industry Research Institute

CF01 Termination of patent right due to non-payment of annual fee
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20060111