Classifications

• • C—CHEMISTRY; METALLURGY
  • C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
  • C09D—COATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
  • C09D163/00—Coating compositions based on epoxy resins; Coating compositions based on derivatives of epoxy resins
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
  • C08G18/00—Polymeric products of isocyanates or isothiocyanates
  • C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
  • C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
  • C08G18/40—High-molecular-weight compounds
  • C08G18/48—Polyethers
  • C08G18/50—Polyethers having heteroatoms other than oxygen
  • C08G18/5096—Polyethers having heteroatoms other than oxygen containing silicon
• • C—CHEMISTRY; METALLURGY
  • C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
  • C09D—COATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
  • C09D5/00—Coating compositions, e.g. paints, varnishes or lacquers, characterised by their physical nature or the effects produced; Filling pastes
  • C09D5/44—Coating compositions, e.g. paints, varnishes or lacquers, characterised by their physical nature or the effects produced; Filling pastes for electrophoretic applications
  • C09D5/4419—Coating compositions, e.g. paints, varnishes or lacquers, characterised by their physical nature or the effects produced; Filling pastes for electrophoretic applications with polymers obtained otherwise than by polymerisation reactions only involving carbon-to-carbon unsaturated bonds
  • C09D5/443—Polyepoxides
  • C09D5/4434—Polyepoxides characterised by the nature of the epoxy binder
  • C09D5/4438—Binder based on epoxy/amine adducts, i.e. reaction products of polyepoxides with compounds containing amino groups only
• • C—CHEMISTRY; METALLURGY
  • C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
  • C09D—COATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
  • C09D5/00—Coating compositions, e.g. paints, varnishes or lacquers, characterised by their physical nature or the effects produced; Filling pastes
  • C09D5/44—Coating compositions, e.g. paints, varnishes or lacquers, characterised by their physical nature or the effects produced; Filling pastes for electrophoretic applications
  • C09D5/4419—Coating compositions, e.g. paints, varnishes or lacquers, characterised by their physical nature or the effects produced; Filling pastes for electrophoretic applications with polymers obtained otherwise than by polymerisation reactions only involving carbon-to-carbon unsaturated bonds
  • C09D5/443—Polyepoxides
  • C09D5/4457—Polyepoxides containing special additives, e.g. pigments, polymeric particles

Definitions

• This invention is directed to a cathodic electrocoating composition and in particular to a cathodic electrocoating composition containing an anticrater agent which significantly reduces craters and improves the smoothness of an electrodeposited film of the composition.
• the coating of electrically conductive substrates by an electrodeposition process also called an electrocoating process is a well known and important industrial process. Electrodeposition of primers to automotive substrates is widely used in the automotive industry. In this process, a conductive article, such as an autobody or an auto part, is immersed in a bath of a coating composition of an aqueous emulsion of film forming polymer and acts as an electrode in the electrodeposition process.
• An electric current is passed between the article and a counter-electrode in electrical contact with the aqueous emulsion, until a desired coating is deposited on the article.
• the article to be coated is the cathode and the counter-electrode is the anode.
• Resin compositions used in the bath of a typical cathodic electrodeposition process also are well known in the art. These resins typically are made from polyepoxide resins which have been chain extended and then an adduct is formed to include amine groups in the resin. Amine groups typically are introduced through reaction of the resin with an amine compound. These resins are blended with a crosslinking agent and then neutralized with an acid to form a water emulsion which is usually referred to as a principal emulsion.
• the principal emulsion is combined with a pigment paste, coalescent solvents, water, and other additives to form the electrocoating bath.
• the electrocoating bath is placed in an insulated tank containing the anode.
• the article to be coated is the cathode and is passed through the tank containing the electrodeposition bath.
• the thickness of the coating that is deposited on the article being electrocoated is a function of the bath characteristics, the electrical operating characteristics of the tank, the immersion time, and the like.
• the resulting coated article is removed from the bath after a set period of time and is rinsed with deionized water.
• the coating on the article is cured typically in an oven at sufficient temperature to produce a crosslinked finish on the article.
• Cathodic electrocoating compositions, resin compositions, coating baths and cathodic electrodeposition processes are disclosed in Jarabek et al US 3,922,253 issued November 25, 1975; Wismer et al US 4,419,467 issued December 6, 1983; Belanger US 4,137,140 issued January 30, 1979 and Wismer et al US 4,468,307 issued August 25, 1984.
• a continuing problem with cathodic electrocoating compositions has been the presence of craters in the cured finish.
• An additive or agent is needed for electrocoating compositions so that crater-free, smooth and even finishes are formed on electrodeposition and curing.
• An improved aqueous cathodic electrocoating composition having a binder of an epoxy-amine adduct and a blocked polyisocyanate crosslinking agent; wherein the improvement is the use of an anticrater agent which is a silane terminated reaction product of polyoxyalkylene diamine and a glycidoxy alkyl alkoxy silane which is hydrolyzed and the anticrater agent has a number average molecular weight ratio of about 700-5,000 determined by Gel Permeation Chromatography (GPC) using polystyrene as the standard.
• GPC Gel Permeation Chromatography
• the novel anticrater agent is readily incorporated into the electrocoating composition by dispersing it with a nonionic surfactant in water and then adding it to an aqueous electrocoating composition since it is compatible with the other constituents of the composition.
• the anticrater agent remains stable in the composition and in the electrocoating bath for extended periods of time under conventional bath operating conditions since it is not reactive with the other constituents in the composition.
• the anticrater agent significantly reduces and often eliminates craters in electrodeposited coatings and forms smooth and even finishes does not migrate to the surface on baking of the finish.
• the additive does not adversely affect other properties of the electrocoating bath or finishes of the electrocoating composition.
• the anticratering agent can be used as a rheology control agent to improve edge protection of an electrodeposited finish.
• the anticrater additive is used in an electrocoating composition in a sufficient amount to significantly reduce or eliminate cratering in the electrodeposited finish.
• the anticrater agent is used in the electrocoating composition at a level of at least 0.5% by weight, based on the total weight of binder solids in the electrocoating composition and preferably, it is used at a level of about 0.5-10% by weight. More preferably, about 1-5% by weight of the anticrater agent is used.
• the binder of the electrocoating composition typically is a blend of an epoxy amine adduct and a blocked polyisocyanate crosslinking agent.
• the anticrater agent is prepared by reacting a polyoxyalkylene diamine with glycidoxy alkyl alkoxy silane in a 1 :2 molar ratio to form an anticratering agent having terminal silane groups. These constituents are reacted at a temperature of about 50 to 130°C for about 1 to 5 hours until there is no residual epoxy present and subsequently hydrolzed.
• the anticrater agent has a number average molecular weight of about 700-5,000.
• the polyoxyalkylene diamine used to form the anticrater agent has 2-4 carbon atoms in the alkylene group and preferably is polyoxypropylene diamine having number average molecular weight of about 230-3,000 preferably, 1,500 - 2,500 such as Jeffamine D-2000 ® having a number average molecular weight of about 2000 available from Huntsman Corporation.
• Another polyoxyalkylene diamine that can be used is polyoxyethylene diamine having a similar molecular weight.
• Typically useful glycidoxy alkyl alkoxy silanes have the formula
• Typical silanes are gamma-glycidoxy propyl trimethoxy silane, gamma-glycidoxy ethyl trimethoxy silane, gamma-glycidoxy methyl trimethoxy silane, gamma-glycidoxy methyl triethoxy silane, gamma-glycidoxy ethyl triethoxy silane, gamma-glycidoxy propyl triethoxy silane.
• Gamma-glycidoxy propyl trimethoxy silane is preferred to form a high quality anticrater agent.
• the anticrater agent can be added to the electrocoating composition at almost any time. It can be added to the principal emulsion, or to the bath the anticrater agent is blended with a nonionic surfactant and an acid such as lactic acid and dispersed in water until hydrolysis of silane group to silanol groups is completed and then added to the electrocoating composition as indicated above.
• the anticrater agent after complete hydrolysis has the following structural formula:
• the anticrater agent is potentially usable with a variety of different cathodic electrocoat resins, but the preferred resin is the typical epoxy-amine adduct of the prior art. These resins are generally disclosed in U. S. Patent No.
• Typical acids used to neutralize the epoxy-amine adduct to form water dispersible cationic groups are lactic acid, acetic acid, formic acid, sulfamic acid, alkane sulfonic acids such as methane sulfonic acid and the like.
• Preferred crosslinkers for the above resins are also well known in the prior art. These are aliphatic, cycloaliphatic and aromatic isocyanates such as hexamethylene diisocyanate, cyclohexamethylene diisocyanate, toluene diisocyanate, methylene diphenyl diisocyanate and the like.
• isocyanates are pre-reacted with a blocking agent such as oximes, alcohols, or caprolactams which block the isocyanate functionality, i.e., the crosslinking functionality. Upon heating the blocking agents separate, thereby providing a reactive isocyanate group and crosslinking occurs.
• a blocking agent such as oximes, alcohols, or caprolactams which block the isocyanate functionality, i.e., the crosslinking functionality.
• the cathodic binder of the epoxy amine adduct and the blocked isocyanate are the principal resinous ingredients in the electrocoating composition and are usually present in amounts of about 30 to 50 % by weight of solids of the composition. To form an electrocoating bath, the solids are generally reduced with an aqueous medium.
• the electrocoating composition usually contains pigment which is incorporated into the composition in the form of a pigment paste.
• the pigment paste is prepared by grinding or dispersing a pigment into a grinding vehicle and optional ingredients such as wetting agents, surfactants, and defoamers. Any of the pigment grinding vehicles that are well known in the art can be used or the anticrater agent of this invention can be used. .After grinding, the particle size of the pigment should be as small as practical, generally, the particle size is about 6-8 using a Hegman grinding gauge. Pigments which can be used in this invention include titanium dioxide, basic lead silicate, strontium chromate, carbon black, iron oxide, clay and the like.
• Pigments with high surface areas and oil absorbencies should be used judiciously because these can have an undesirable affect on coalescence and flow of the electrodeposited coating.
• the pigment to binder weight ratio is also important and should be preferably less than 0.5: 1, more preferably less than 0.4: 1, and usually about 0.2 to 0.4: 1. Higher pigment to binder weight ratios have been found to adversely affect coalescence and flow.
• the coating compositions of the invention can contain optional ingredients such as wetting agents, surfactants, defoamers and the like.
• surfactants and wetting agents include alkyl imidazolines such as those available from Ciba-Geigy Industrial Chemicals as "Amine C", acetylenic alcohols available from Air Products and Chemicals as "Surfynol 104".
• These optional ingredients when present, constitute from about 0.1 to 20 percent by weight of binder solids of the composition.
• plasticizers can be used to promote flow. Examples of useful plasticizers are high boiling water immiscible materials such as ethylene or propylene oxide adducts of nonyl phenols or bisphenol A.
• the electrocoating composition of this invention is an aqueous dispersion.
• the term "dispersion" as used within the context of this invention is believed to be a two-phase translucent or opaque aqueous resinous binder system in which the binder is in the dispersed phase and water the continuous phase.
• the average particle size diameter of the binder phase is about 0.1 to 10 microns, preferably, less than 5 microns.
• the concentrations of the binder in the aqueous medium in general is not critical, but ordinarily the major portion of the aqueous dispersion is water.
• the aqueous dispersion usually contains from about 3 to 50 percent preferably 5 to 40 percent by weight binder solids.
• Aqueous binder concentrates which are to be further diluted with water when added to an electrocoating bath, generally have a range of binder solids of 10 to 30 percent weight.
• the anticrater agent was prepared by charging 996.5 parts of Jeffamine D2000 ® (polyoxypropylene diamine having a number molecular weight of 2000 and an amine equivalent of 996.5) and 236 parts of gamma-glycidoxy propyltrimethoxy silane. The reaction mixture was heated to about 59°C until the epoxy equivalent weight was greater than 40,000. The resulting adduct was then dispersed by combining 35 parts acetic acid and 4,900 parts deionized water and agitated until there was complete hydrolysis of silane groups to silanol groups. The resulting adduct solution had a nonvolatile content of 20%.
• An alcohol blocked polyisocyanate crosslinking resin solution was prepared by charging 317.14 parts of PAPI 2027 ® (methylene diphenyl diisocyanate), 47.98 parts of methyl isobutyl ketone and 0.064 parts of dibutyl tin dilaurate into a suitable reaction vessel and heated to 37°C under a nitrogen blanket. A mixture of 323.10 parts of diethylene glycol mono butyl ether and 13.04 parts of trimethylolpropane was slowly charged into the reaction vessel while maintaining the reaction mixture below 93 °C for an additional hour until essentially all of the isocyanate was reacted as indicated by infrared scan of the reaction mixture. 2.30 parts of butanol and 167.37 parts of methyl isobutyl ketone were added. The resulting resin solution had a nonvolatile content of 75%. Preparation of OuaterniTing Agent
• the quaternizing agent was prepared by adding 87 parts dimethylethanolamine to 320 parts ethylhexanol half-capped toluene diisocyanate in the reaction vessel at room temperature. An exothermic reaction occured and the reaction mixture was stirred for one hour at 80°C. 118 parts aqueous lactic acid solution (75% nonvolatile content) was then added followed by the addition of 39 parts 2-butoxyethanol. The reaction mixture was held for about one hour at 65°C with constant stirring to form quaternizing agent.
• the pigment grinding vehicle was prepared by charging 710 parts Epon 829 ® (diglycidyl ether of bisphenol A having an epoxide equivalent weight of 193-203) and 290 parts bisphenol A into a suitable vessel under nitrogen blanket and heated to 150-160°C to initiate an exothermic reaction. The exothermic reaction was continued for about one hour at 150-160°C. The reaction mixture was then cooled to 120° and 496 part of 2-ethylhexanol half capped toluene diisocyanate was added.
• Epon 829 ® diglycidyl ether of bisphenol A having an epoxide equivalent weight of 193-203
• the exothermic reaction was continued for about one hour at 150-160°C.
• the reaction mixture was then cooled to 120° and 496 part of 2-ethylhexanol half capped toluene diisocyanate was added.
• the temperature of the reaction mixture was held at 110- 120°C for one hour, followed by the addition of 1095 parts of 2-butoxyethanol, the reaction mixture was then cooled to 85-90°C and then 71 parts of deionized water was added followed by the addition of 496 parts quarternizing agent (prepared above). The temperature of the reaction mixture was held at 85-90°C until an acid value of about 1 was obtained.
• Pigment grinding vehicle (prepared above) 812 Deionized water 1660
• the above ingredients were mixed until homogenous mixture was formed in a suitable mixing container. Then were dispersed by charging the mixture into a sand mill and then grinding untila Hegman reading of seven or greater was obtained.
• a Cationic electrocoating Bath I and ⁇ were prepared by mixing the above ingredients. Each bath was then ultrafiltered. Each bath was electrocoated at 250-270 volts to obtain 0.9-1.0 mils (22.86-25.4 microns). ASPP blow out crater test is used to test each bath. Crater resistance was rated according to the following rating scale of A-E:
• the crater resistant rating for both Baths I and II was A.
• An electrocoating bath was prepared identical to Bath I above except the anticrater agent was replaced with a conventional anti cratering agent which is the reaction product of Jeffamine ® 2000 and Epon ® 1001 epoxy resin and the crater resistance of this bath was tested as above by using the ASPP blow out crater test.
• the crater resistance rating for this panel was E which is substantially inferior to the panels coated in Baths I and II which contained the anticrater agent of this invention.
• knife blades (10 x 2 cm) were electrocoated in Baths I and II at 250 volts and baked at 182°C (metal temperature) for 10 minutes. The knife blades then were exposed to salt spray for 7 days. The number of rust spots on each blade were counted by viewing the blades under a microscope. The blades from Bath I had 100-120 rust spots while the blades from Bath ⁇ had 20-40 rust spots which shows that Bath II which contained three times the amount of anticratering agent provided better edge corrosion protection.

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• Chemical & Material Sciences (AREA)
• Life Sciences & Earth Sciences (AREA)
• Organic Chemistry (AREA)
• Chemical Kinetics & Catalysis (AREA)
• Materials Engineering (AREA)
• Engineering & Computer Science (AREA)
• Wood Science & Technology (AREA)
• Health & Medical Sciences (AREA)
• Molecular Biology (AREA)
• Medicinal Chemistry (AREA)
• Polymers & Plastics (AREA)
• Paints Or Removers (AREA)
• Polyethers (AREA)

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• 1997
  • 1997-02-25 US US08/806,868 patent/US5723519A/en not_active Expired - Fee Related
  • 1997-10-22 US US08/956,223 patent/US5883276A/en not_active Expired - Fee Related
• 1998
  • 1998-02-18 BR BR9807378-8A patent/BR9807378A/pt not_active IP Right Cessation
  • 1998-02-18 JP JP53683598A patent/JP2001512520A/ja not_active Withdrawn
  • 1998-02-18 DE DE69802266T patent/DE69802266T2/de not_active Expired - Lifetime
  • 1998-02-18 KR KR10-1999-7007684A patent/KR100510229B1/ko not_active Expired - Fee Related
  • 1998-02-18 WO PCT/US1998/003134 patent/WO1998037155A1/en not_active Ceased
  • 1998-02-18 CA CA002279872A patent/CA2279872A1/en not_active Abandoned
  • 1998-02-18 AU AU61738/98A patent/AU739053B2/en not_active Ceased
  • 1998-02-18 EP EP98906541A patent/EP0963417B1/en not_active Expired - Lifetime
  • 1998-02-18 CN CNB988027488A patent/CN1156543C/zh not_active Expired - Fee Related

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