http://rdf.ncbi.nlm.nih.gov/pubchem/patent/TW-201242945-A

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assignee http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_461514df460e0cdd5644e86ba60adbf7
classificationIPCInventive http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C67-54
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01D3-42
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C29-82
filingDate 2011-04-28-04:00^^<http://www.w3.org/2001/XMLSchema#date>
inventor http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_c78f6019b43158e549b945f122084390
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_69c3b1cea5db9f7577410016962c5633
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_62018e4e96abb447ad6c727b24b480f8
publicationDate 2012-11-01-04:00^^<http://www.w3.org/2001/XMLSchema#date>
publicationNumber TW-201242945-A
titleOfInvention Heterogeneous azeotropic distillation method
abstract A heterogeneous azeotropic distillation method, which requires only one distillation column, is provided. The distillation column includes a first distillation section and a second distillation section. The first distillation section is on top of the second section. In the disclosed heterogeneous azeotropic distillation method, a mixture which includes methyl methacrylate, methanol, and water is transported into the distillation column. The mixture is distilled at a temperature between 65 DEG C and 106 DEG C. A liquid stream in the end of the first section is drawn out and cooled down to form a water-rich phase and an organic-rich phase. Then, the organic-rich phase is transported back to the end of the first distillation section. In the heterogeneous azeotropic distillation method, only one distillation column is needed to obtain a high-purity methyl methacrylate. Hence the cost of the equipments and the floor space of plant site are both reduced.
priorityDate 2011-04-28-04:00^^<http://www.w3.org/2001/XMLSchema#date>
type http://data.epo.org/linked-data/def/patent/Publication

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