82601-55-6

Basic information

• Product Name: 2-hydroxyethyl 2-methylprop-2-enoate
• Synonyms: 2-hydroxyethyl 2-methylprop-2-enoate
• CAS NO: 82601-55-6
• Molecular Formula: C6H10O3
• Molecular Weight: 130.14
• Mol File: 82601-55-6.mol
• Article Data: 36

Chemical Properties

• Appearance: /
• CAS DataBase Reference: 2-hydroxyethyl 2-methylprop-2-enoate(CAS DataBase Reference)
• NIST Chemistry Reference: 2-hydroxyethyl 2-methylprop-2-enoate(82601-55-6)
• EPA Substance Registry System: 2-hydroxyethyl 2-methylprop-2-enoate(82601-55-6)

Safety Data

• Hazardous Substances Data: 82601-55-6(Hazardous Substances Data)

Upstream product

• 75-21-8 oxirane 
• 79-41-4 poly(methacrylic acid) 
• 107-21-1 ethylene glycol 
• 80-62-6 methacrylic acid methyl ester 
• 107-07-3 2-chloro-ethanol 
• 6900-35-2 potassium methacrylate 
• 920-46-7 Methacryloyl chloride 
• 463-49-0 1,2-propanediene 
• 201230-82-2 carbon monoxide 
• 80-55-7 ethyl 2-hydroxy-2,2-dimethylethanoate 
• 594-61-6 2-methyllactic acid 
• 2110-78-3 methyl 2-hydroxy-2-methylpropionate 
• 92-84-2 10H-phenothiazine 
• 2421-28-5 dianhydride of benzophenone-3,4,3',4'-tetracarboxy acid 

Downstream Products

• 19117-13-6 2-Methyl-acrylic acid 2-(heptyl-{4-[1-(4-{heptyl-[2-(2-methyl-acryloyloxy)-ethoxy]-phosphinoyloxy}-phenyl)-1-methyl-ethyl]-phenoxy}-phosphinoyloxy)-ethyl ester 
• 105501-11-9 sodium 2,3-bis(hexadecyloxy)propyl 3-methacryloyl-3-oxapropyl phosphate 
• 17407-12-4 dimethyl-di(methacroyloxy-1-ethoxy)silane 
• 51293-89-1 2-methylacrylic acid 2-(butylcarbamoyloxy)ethyl ester 
• 102729-29-3 C₂₁H₂₀N₂O₅ 
• 47087-43-4 2-(β-glucosyloxy)ethyl methacrylate 
• 1596353-74-0 C₂₀H₂₀N₂O₅ 
• 1621329-51-8 2-hydroxyethyl (E)-α-methylcinnamate 
• 132153-84-5 2-O-(α-D-mannosyl)hydroxyethyl methacrylate 
• 21698-14-6 2-(β-D-galactosyloxy)ethyl methacrylate 

Relevant articles and documents

Acrylate monomer having hydrophilic end group and a method for preparing the same

More particularly, the present invention relates to an acrylate monomer having a high-purity hydrophilic terminal group which does not contain unreacted 1 water or undesirable by-products, and a method for producing the acrylate monomer. These acrylate monomers are substantially free of polymerization inhibitors. Chemical Formula 1. In Chemical Formula 1, R. 1 Chem. R. 2 Chem. R. 3 May be H, or linear, branched or cyclic C, independently of each other. 1 -C12 alkyl group. R4 Is linear, branched or cyclic C. 1 -C12 alkyl Or C1 -C12 It is alkoxy group, wherein alkyl group carbon atoms can be unsubstituted or substituted with oxygen atoms, n Is an integer selected from 1 and 10.

Runge-Kutta analysis for optimizing the Zn-catalyzed transesterification conditions of MA and MMA with diols to maximize monoesterified products

Terminal hydroxylated acrylates and methacrylates were prepared by catalytic transesterification of acrylates and methacrylates with diols catalyzed by a system of a tetranuclear zinc alkoxide, [Zn(tmhd)(OMe)(MeOH)]4 (1a), with 4 equiv. of 2,2′-bipyridine (L1). The reaction time to reach the equilibrium state was analyzed by kinetic studies and a curve-fitting analysis based on the Runge-Kutta method for optimizing the best reaction conditions for mono-esterification. In addition to these kinetic analyses, DFT calculations estimated a proposed mechanism of the catalytic transesterification. This journal is

METHOD FOR PREPARING HYDROXYETHYL (METH) ACRYLATE

Hydroxyethyl (methyl)acrylate is prepared by a process of a combination of a three-stage tubular reactor and a tower reactor, wherein, firstly, a catalyst, a polymerization inhibitor and (methyl) acrylic acid are mixed until the solids are dissolved, then mixed with a part of ethylene oxide and thereafter enter into a first tubular reactor for a reaction, a reaction liquid flowing out from the first tubular reactor is mixed with a certain amount of ethylene oxide and enters into a second tubular reactor for a reaction, a reaction liquid flowing out from the second tubular reactor is then mixed with a certain amount of ethylene oxide and thereafter enters into a third tubular reactor, and a reaction liquid flowing out from the third tubular reactor is then passed through a stage of an adiabatic tower reactor and aged such that a product liquid is obtained from extraction.