10595-45-6

Usage

Uses

Used in Polymer Production:
N-[2-(diethylamino)ethyl]acrylamide is used as a monomer in the production of polymers for its ability to contribute to the formation of stable and flexible polymer networks.
Used in Cross-linking Agents:
It serves as a cross-linking agent, enhancing the structural integrity and properties of various materials.
Used in Hydrogel Manufacturing:
N-[2-(diethylamino)ethyl]acrylamide is used as a component in the manufacture of hydrogels, which are utilized in various applications due to their unique properties such as water absorption and biocompatibility.
Used in Medical Applications:
In the medical field, N-[2-(diethylamino)ethyl]acrylamide is used in the synthesis of materials for drug delivery systems and tissue engineering due to the hydrogels' properties that can be tailored for specific uses.
Used in Industrial Processes:
N-[2-(diethylamino)ethyl]acrylamide is also utilized in industrial processes where specific polymers with tailored properties are required for various applications, such as in coatings, adhesives, and other material formulations.
It is important to handle N-[2-(diethylamino)ethyl]acrylamide with care due to its potential health hazards and toxicity, similar to acrylamide.

InChI:InChI=1/C9H18N2O/c1-4-9(12)10-7-8-11(5-2)6-3/h4H,1,5-8H2,2-3H3,(H,10,12)

Upstream product

• 100-36-7 N,N-diethylethylenediamine 
• 625-36-5 2-chloropropionyl chloride 
• 39837-47-3 (diethylamino)ethylamine 
• 865-47-4 potassium tert-butylate 
• 814-68-6 acryloyl chloride 

Relevant academic research and scientific papers

Microspheres useful for therapeutic vascular embolization

Provided herein, for example, are microspheres comprising a gelatin or gelatin substitute and a copolymer of a N-tris-hydroxymethyl methylacrylamide monomer unit, a diethylaminoethylacrylamide monomer unit and a N,N-methylene-bis-acrylamide monomer unit. Also provided are methods of producing microspheres comprising a gelatin or gelatin substitute and a copolymer of a N-tris-hydroxymethyl methylacrylamide monomer unit, a diethylaminoethylacrylamide monomer unit and a N,N-methylene-bis-acrylamide monomer unit. Further provided herein, for example, are compositions comprising the microspheres and methods of using the microspheres and compositions thereof.

Process for the production of N-substituted acrylic acid amides

The present invention relates to a process for the production of N-substituted acrylic acid amides by conversion of 2-carboalkoxy-t-oxabicyclo(2,2,1)hept-5-enes with primary or secondary amines to 2-carboxamide-7-oxabicyclo(2,2,1)hept-5-enes and the thermal decomposition of the latter, preferably in the presence of Lewis acids and in a vacuum, to furane and N-substituted acrylic acid amides. The process according to the invention results in high purity N-substituted acrylic acid amides that are, in the main, free of bifunctional monomers which would disrupt the subsequent polymerization of the N-substituted acrylic acid amides by undesired cross-linking.

Process for the manufacture of α,β-unsaturated N-substituted carboxylic acid amides

Process for the manufacture of α,β-unsaturated N-substituted carboxylic acid amides of the general formula STR1 in which R1 represents H or CH3 R2 represents H or CH3, and Y represents a divalent straight-chain or branched organic radical having 2-30 carbon atoms, and R3 represents H or the radical of an amine of the formula --N(R4)(R5), in which R4 and R5 represent alkyl radicals having 1 to 4 carbon atoms, by reacting β-substituted carboxylic acid amides of the formula STR2 in which Z represents OH or the radical R6 O--, in which R6 is an alkyl radical having 1 to 4 carbon atoms, with amines of the general formula at temperatures in the range of 100° to 200° C., preferably 120° to 175° C., with the elimination of ammonia, and heating the resulting N-substituted β-hydroxycarboxylic or β-alkoxycarboxylic acid amides in the presence of catalysts, water or alcohol, respectively, being split off. The water is split off at temperatures of 100°-250° C. with acidic catalysts such as phosphoric acid, or basic catalysts such as sodium hydroxide, and alcohol is split off at 70°-150° C. with basic catalysts such as sodium or potassium hydroxide. The reaction product is separated by distillation, optionally in vacuo.