Method of forming composite coating film
a coating film and composite technology, applied in the field of forming composite coating films, can solve the problems of reducing the water resistance of the coating film, difficult to achieve both coat appearance and workability, and poor appearance of the coating film obtained
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production example 1
Production of Resin Emulsion A
[0079] A reactor was charged with 126 parts of deionized water, and the temperature was raised to 80.degree. C. under stirring in a nitrogen atmosphere. Then, a monomer emulsion composed of 100 parts of the .alpha., .beta.-ethylenically unsaturated monomer mixture defined below (acid value: 20; hydroxyl value: 40), 0.5 part of Aqualon HS-10 (polyoxyethylene alkylpropenylphenyl ether sulfate ester, product of Daiichi Kogyo Seiyaku), 0.5 part of Adeka Reasoap NE-20 (.alpha.-[1-[(allyloxy)methyl]-2-(nonylphenoxy)ethyl]-.omega.-hydroxyoxye-thylene, product of Asahi Denka Kogyo) and 100 parts of deionized water and an initiator solution composed of 0.3 part of ammonium persulfate and 10 parts of deionized water were added dropwise in parallel to the reaction vessel over 2 hours. After completion of the dropwise addition, maturation (a ripening reaction) was effected at the same temperature for 2 hours.
[0080] Then, after cooling to 40.degree. C., the reaction...
production example 2
Production of Resin Emulsion B
[0081] A reactor was charged with 136 parts of deionized water and heated to 80.degree. C. Then, under nitrogen with stirring, a monomer emulsion composed of 80 parts of the .alpha., .beta.-ethylenically unsaturated monomer mixture 1 described below, 0.5 part of Aqualon HS-10, 0.5 part of Adeka Reasoap NE-20 and 80 parts of deionized water and an initiator solution composed of 0.24 part of ammonium persulfate and 10 parts of deionized water were added in parallel dropwise over 2 hours. After completion of dropwise addition, a ripening reaction was conducted at the same temperature for 1 hour.
[0082] Then, 20 parts of the .alpha., .beta.-ethylenically unsaturated monomer mixture 2 described below (the acid and hydroxyl values of .alpha., .beta.-ethylenically unsaturated monomer mixtures 1 and 2 combined =20 and 40, respectively) and an initiator solution composed of 0.06 part of ammonium persulfate and 10 parts of deionized water were added in parallel dr...
production example 3
Production of Resin Emulsion C
[0085] Except that the following .alpha., .beta.-ethylenically unsaturated monomer mixture 1 was used (the acid and hydroxyl values of .alpha., .beta.-ethylenically unsaturated monomer mixtures 1 and 2 combined =20 and 40, respectively), the procedure of Production Example 2 was otherwise faithly followed to give the objective resin emulsion C having a mean particle diameter of 280 nm and a nonvolatile fraction of 25%.
4 .alpha., .beta.-Ethylenically unsaturated monomer mixture 1 Methyl methacrylate 5.35 parts Ethyl acrylate 58.23 parts 2-Hydroxyethyl methacrylate 7.42 parts Styrene 5.00 parts Acrylamide 4.00 parts
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