http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-103562192-B

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classificationCPCInventive http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D3-40
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07D303-04
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07D301-19
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07D301-32
classificationIPCInventive http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07D303-04
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07D301-19
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07D301-32
filingDate 2012-06-07-04:00^^<http://www.w3.org/2001/XMLSchema#date>
grantDate 2016-08-17-04:00^^<http://www.w3.org/2001/XMLSchema#date>
publicationDate 2016-08-17-04:00^^<http://www.w3.org/2001/XMLSchema#date>
publicationNumber CN-103562192-B
titleOfInvention Method with extraction distillation column separation oxyalkylene
abstract It relates to thick propylene oxide stream, such as from the intermediate flow of PO/TBA process, the method for separating propylene oxide.Thick propylene oxide stream can be made to pass through extraction distillation column.Distillation column uses C 8 ‑C 20 Alkane, as extractant, with overhead washing drum, operates at a temperature of the pressure more than 25 50psig and/or 70 150 DEG C.Thick propylene oxide stream includes 0.001 0.1% weight percent methanol always formed based on thick propylene oxide stream.Described system, method and apparatus can produce the propylene oxide stream than prior art with less formaldehyde and acetaldehyde.
priorityDate 2011-06-07-04:00^^<http://www.w3.org/2001/XMLSchema#date>
type http://data.epo.org/linked-data/def/patent/Publication

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Total number of triples: 36.