Polyacrylic acid printing ink resin and preparation method thereof
A technology of ink resin and polyacrylic acid, which is applied in the field of printing ink, can solve the problems of severe printing suitability of ink resin, achieve good solvent release, inhibit gel, and ensure controllability
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[0027] Example 1
[0028] Combine 1 kg of methacrylic acid, 41 kg of methyl methacrylate, 40 kg of styrene, 1 kg of maleic acid, 15 kg of rosin, 1 kg of isopropanol, 1 kg of azobisisobutyl The nitrile is uniformly mixed in the feed tank to obtain the reaction material, and then the reaction material is pumped into a tubular reactor equipped with a static mixing device for continuous bulk polymerization; during continuous bulk polymerization, the temperature of the tubular reactor is 100 The temperature is ℃, the pressure is 0.5MPa, and the residence time of the reaction material in the tubular reactor is 40 minutes; after the reaction product is discharged, the polyacrylic acid ink resin with a number average molecular weight of 70,000 is obtained by extraction and granulation.
Example Embodiment
[0029] Example 2
[0030] Combine 10 kg of acrylic acid, 10 kg of methacrylic acid, 12 kg of butyl acrylate, 18 kg of pentyl acrylate, 21 kg of vinyl butyrate, 9 kg of methyl styrene, 10 kg of itaconic acid, 5.5 kg of acrylonitrile, 1 kg of rosin phenolic resin, 1 kg of epoxy resin, 0.3 kg of propylene glycol, 0.2 kg of thioglycolic acid, 0.5 kg of benzoyl peroxide, 1.5 kg of dicumyl peroxide The reaction materials are uniformly mixed in the feed tank, and then the reaction materials are pumped into a tubular reactor equipped with a static mixing device for continuous bulk polymerization; during continuous bulk polymerization, the temperature of the tubular reactor is 300°C, The pressure is 4MPa, and the residence time of the reaction material in the tubular reactor is 2 minutes; after the reaction product is discharged, the polyacrylic acid ink resin with a number average molecular weight of 10,000 is obtained through extraction and granulation.
Example Embodiment
[0031] Example 3
[0032] Combine 7 kg of acrylic acid, 3.5 kg of methacrylic acid, 10 kg of isobutyl acrylate, 40 kg of nonyl methacrylate, 5 kg of vinyl laurate, 15 kg of ethylene tertiary carbonate, and 5 kg of acrylic acid. -2-hydroxyethyl, 7 kg of acrylamide, 1 kg of cellulose, 2 kg of polycarbonate, 0.1 kg of mercaptohexanol, 0.4 kg of 3-mercaptopropionic acid, 2.5 kg of diacetyl peroxide, 1.5 kg of tert-butyl peroxylaurate is mixed uniformly in the feed tank to obtain the reaction material, and then the reaction material is pumped into a tubular reactor equipped with a static mixing device for continuous bulk polymerization; in continuous bulk polymerization When the temperature of the tubular reactor is 200℃, the pressure is 3.5MPa, the residence time of the reaction materials in the tubular reactor is 30 minutes; after the reaction products are discharged, they are extracted and granulated to obtain the number average molecular weight It is 50,000 polyacrylic ink resin....
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