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Controlled radical polymerization of (meth)acrylic monomers

A free-radical, acrylic technology for use in ester copolymer adhesives, adhesive types, coatings, etc. to address undesired characteristics, poor rheological control, unpredictable properties, etc.

Active Publication Date: 2015-07-01
HENKEL KGAA
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The molecular weight and polydispersity index of the product differ from theory due to premature termination of the polymer ends, which often leads to poor rheological control and impracticality of various applications and uses
Consequently, the lack of control in the ATRP process results in polymer products with structural defects, less desirable features, and less predictable properties
Additionally, Cu(I) salts are unstable in air and require careful handling

Method used

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  • Controlled radical polymerization of (meth)acrylic monomers
  • Controlled radical polymerization of (meth)acrylic monomers
  • Controlled radical polymerization of (meth)acrylic monomers

Examples

Experimental program
Comparison scheme
Effect test

Embodiment

[0042] Comparative Example - Using dimethyl 2,6-dibromopimelate / Cu(0) / pentamethyldiethylenetriamine in acetonitrile One-pot synthesis of polymethyl acrylate

[0043]34g acetonitrile, 0.670g dimethyl 2,6-dibromopimelate, 0.0697g pentamethyldiethylenetriamine (PMDETA) and 31.82g methyl acrylate were added with mechanical stirrer, two condensers and a rubber septum in a 250 ml four-neck round bottom flask. The mixture was stirred and cooled to -78°C, and 53 g of copper mesh treated with 0.1N hydrochloric acid was added to the mixture with continuous stirring. The flasks were then degassed using 6 freeze-pump-thaw cycles under nitrogen. Then, the reaction mixture was heated to 25°C and the polymerization was continued for 4 hours and stopped by introducing air.

[0044] The product sample was dissolved in deuterated chloroform (CDCl 3 ), and through 1 Conversion was measured by H-NMR spectroscopy. At 4 hours, the conversion of methyl acrylate was 72%. The samples were di...

Embodiment 4

[0057] Inventive Example 4 - Using PhCHBr 2 / Cu(0) / pentamethyldiethylenetriamine in acetonitrile polymethyl acrylate

[0058]

[0059] Using the method of the present invention, 34.05 g of acetonitrile, 0.530 g of a,a-dibromotoluene and 1.03 g of copper mesh treated with 0.1N hydrochloric acid were added to a 250 ml necked round bottom flask. 0.0798 g PMDETA and 31.41 g methyl acrylate were added to a 50 ml Schlenk tube. Both mixtures were degassed through 6 freeze-pump-thaw cycles under nitrogen. The methyl acrylate / PMDETA mixture was added dropwise to the flask at 45°C under nitrogen through a cannula over 30 minutes. The polymerization reaction continued for 4 hours and was stopped by introducing air.

[0060] Samples were taken at various intervals throughout the polymerization. Dissolve the sample in CDCl 3 in and through 1 Conversion was measured by H-NMR spectroscopy. At 4 hours, the conversion of methyl acrylate was 79%. The samples were dissolved i...

Embodiment 5

[0061] Inventive Example 5 - Using PhCHBr 2 / Cu(0) / pentamethyldiethylenetriamine in acetonitrile 2-ethylhexyl polyacrylate

[0062]

[0063] Using the method of the present invention, 37.60 g of acetonitrile, 1.2491 g of a,a-dibromotoluene and 0.56 g of copper mesh treated with 0.1N hydrochloric acid were added to a 250 ml necked round bottom flask. 0.0770 g PMDETA and 37.60 g 2-ethylhexyl acrylate were added to a 50 ml Schlenk tube. Both mixtures were degassed through 6 freeze-pump-thaw cycles under nitrogen. The 2-ethylhexyl acrylate / PMDETA mixture was added dropwise to the flask via cannula at 45°C under nitrogen over 60 minutes. The polymerization reaction continued for 3.5 hours and was stopped by introducing air.

[0064] Samples were taken at various intervals throughout the polymerization. Dissolve the sample in CDCl 3 in and through 1 Conversion was measured by H-NMR spectroscopy. At 4 hours, the conversion of 2-ethylhexyl acrylate was 54%. The sam...

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Abstract

Living radical polymerization processes, reaction products of such processes, and compositions containing such reaction products are provided. More particularly, a living radical polymerization of (meth)acrylic acid monomers employing having a defined order of introduction of the reactants and / or a specific set of reaction conditions, is provided.

Description

technical field [0001] The present invention relates to controlled free radical polymerization processes, reaction products of such processes, and compositions containing such reaction products. More specifically, the present invention relates to a process for the controlled free radical polymerization of acrylic and / or methacrylic monomers using a defined sequence of reactant introduction and / or a specific set of reaction conditions. Background technique [0002] The need for more efficient methods of making polymers continues. Controlled Radical Polymerization ("CRP"), including Single Electron Transfer Living Radical Polymerization ("SET-LRP") and Atom Transfer Living Radical Polymerization ("ATRP"), are prepared in high yields with functionalized non-terminating ends , Process for various polymer products with high molecular weight and with low polydispersity index. Therefore, CRP has been used to design various polymer products. However, these CRP processes often req...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C08F2/38C08F2/00C08F20/10C09J133/04C09D133/04
CPCC08F20/18C08F220/14C08F4/00C08F2/38C08F2438/01C08F20/14C08F4/06C08F220/26C08F220/20C08F220/18C08F220/1804C08F220/1808
Inventor 朱勤艳D·P·德沃劳克J·G·伍兹A·F·雅各宾
Owner HENKEL KGAA