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

Active Publication Date: 2014-09-10
INST OF CHEM CHINESE ACAD OF SCI
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

However, the ink resin prepared with this

Method used

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  • Polyacrylic acid printing ink resin and preparation method thereof
  • Polyacrylic acid printing ink resin and preparation method thereof

Examples

Experimental program
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Example Embodiment

[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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Abstract

The invention belongs to the field of printing ink and specifically relates to polyacrylic acid printing ink resin and a preparation method thereof. The preparation method comprises the steps of uniformly mixing (methyl) acrylic acid, (methyl) acrylate, a vinyl monomer, an active functional monomer, an auxiliary component, a molecular weight regulator and an initiator in a feeding tank to obtain reaction materials; then, pumping the reaction materials into a tubular reactor in which a static mixing device is arranged, and preparing polyacrylic acid printing ink resin at a high temperature under high pressure by adopting a continuous main body polymerization method, wherein the adopted continuous main body polymerization process effectively inhibits occurrence of gelling and implosion reaction in a main body polymerization process, ensures controllability of molecular weight of the polyacrylic acid printing ink resin, and prepares the polyacrylic acid printing ink resin with number-average molecular weight of 10000-70000. The polyacrylic acid printing ink disclosed by the invention has good solvent release property and printing adaptation.

Description

technical field [0001] The invention belongs to the field of printing ink, in particular to polyacrylic acid ink resin for printing and a preparation method thereof. Background technique [0002] In recent years, with the diversification of packaging requirements and the development of packaging technology, various plastic films have emerged as packaging materials. Plastic films for packaging often require printing for reasons of decoration or surface protection. Plastic gravure ink is a coloring material used for plastic packaging printing. [0003] In recent years, the ester-soluble and alcohol-soluble polyurethane plastic gravure inks that have appeared on the market have problems such as high price and poor wetting and dispersibility of pigments, which have affected the popularization and use of such products. [0004] In view of this, researchers are developing more and more alcohol-soluble acrylic ink resins. For example, Chinese patent CN101747475B discloses a synth...

Claims

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Application Information

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IPC IPC(8): C08F220/14C08F220/18C08F212/08C08F220/06C08F222/02C08F218/10C08F220/46C08F218/00C08F220/56C08F216/14C08F220/34C08F220/28C08F2/38C09D11/107
Inventor 王旭朋宋延林王丽李阳
Owner INST OF CHEM CHINESE ACAD OF SCI
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