http://rdf.ncbi.nlm.nih.gov/pubchem/patent/FR-2839070-A1

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classificationCPCInventive http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C213-06
classificationIPCInventive http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C213-06
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C219-08
filingDate 2002-04-30-04:00^^<http://www.w3.org/2001/XMLSchema#date>
inventor http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_a26a7065f48e3ee0c13c6afe6efff52b
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_5e3ca8a0d4ec232be5d22c309af2b05c
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_5d0779013373b97870fa67917c34279b
publicationDate 2003-10-31-04:00^^<http://www.w3.org/2001/XMLSchema#date>
publicationNumber FR-2839070-A1
titleOfInvention PROCESS FOR THE CONTINUOUS MANUFACTURE OF DIMETHYLAMINOETHYL ACRYLATE
abstract Dimethylaminoethyl acrylate is produced by transesterification from dimethylaminoethanol and ethyl acrylate, in the presence of a transesterification catalyst and at least one polymerization inhibitor, the azeotropic mixture of ethyl acrylate-ethanol being continuously withdrawn during the reaction. According to the invention, the reaction is carried out by implementing the technology in a tubular piston reactor. In particular, several tubular piston reactors are used, mounted in series (R1, R2, R3), the reaction mixture being injected at the base of the first reactor (R1) and leaving at the top of it to be reinjected at the base of the second reactor (R2) and so on, the aforementioned azeotropic mixture leaving at the top of each reactor (R1, R2, R3) being injected in a distillation column (C) equipped with a condenser.
isCitedBy http://rdf.ncbi.nlm.nih.gov/pubchem/patent/FR-2876375-A1
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/WO-2006040470-A1
priorityDate 2002-04-30-04:00^^<http://www.w3.org/2001/XMLSchema#date>
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