14144-48-0Relevant articles and documents
PROCESS FOR PRODUCING -ALKOXYPROPIONAMIDE
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Page/Page column 6, (2009/12/07)
A method for producing a β-alkoxypropionamide shown by the following formula (I) including the step of reacting a β-alkoxypropionic acid ester with an amine in the presence of a basic catalyst or in the presence of a basic catalyst and a polyol: wherein R1 is an alkyl group having 1 to 8 carbon atoms, and R2 and R3 are independently hydrogen, a methyl group, an ethyl group, a methoxy group, an ethoxy group, a methoxymethyl group or a glycidyl group.
PROCESS FOR THE MANUFACTURE OF C1 -C4 ALKYL (METH)ACRYLATES
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Page/Page column 4, (2008/06/13)
The invention relates to an improved process for the manufacture of C1-C4 alkyl (meth)acrylates by a direct esterification of (meth)acrylic acid by the corresponding alcohol in the presence of sulphuric acid, phenothiazine being used as polymerization inhibitor. The said process comprises a stage of recovering in value the heavy byproducts generated during this manufacture which consists of a distillation at a relatively low temperature and under an inert atmosphere, followed by a catalytic cracking under an inert atmosphere.
METHODS OF MANUFACTURING DERIVATIVES OF β-HYDROXYCARBOXYLIC ACIDS
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Page/Page column 14-15, (2008/06/13)
Preparation of derivatives of β-hydroxycarboxylic acid, including β-hydroxycarboxylic acid esters, α,β-unsaturated carboxylic acids, esters of α,β-unsaturated carboxylic acid, and alkoxy derivatives.
Process for preparing butyl acrylate by direct esterification
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Page/Page column 2-3, (2008/06/13)
Butyl acrylate is prepared by reacting acrylic acid and butanol in a reactor in the presence of an esterification catalyst the water formed being entrained by distillation in a column (2) in the form of a heteroazeotropic mixture with butanol mixture following condensation, being separated in a decanter (3) to give an upper, organic phase which is recycled to the top of the distillation column (2) and a lower, aqueous phase which is drawn off. The reaction is conducted with deferred introduction of part of the butanol at the top of the distillation column (2) or to the decanter (3) or to the reactor (1), the butanol/acrylic acid molar ratio being initially between 0.5 and 1 before rising to between 1 and 1.5 following the completion of the deferred introduction of the butanol.
Transesterification of alkoxyesters
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, (2008/06/13)
Method for the highly selective transesterification of alkyl 3-alkoxypropionates, as well as several novel alkoxypropionate compounds, are provided. Transesterification catalyzed by titanium alkoxides or tin compounds does not catalyze the Michael reaction, and therefore, provide highly selective transesterification reactions of these reactive materials.