http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-206256006-U

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classificationIPCInventive http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C29-00
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C29-80
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C29-78
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C35-30
filingDate 2016-11-24-04:00^^<http://www.w3.org/2001/XMLSchema#date>
grantDate 2017-06-16-04:00^^<http://www.w3.org/2001/XMLSchema#date>
inventor http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_78fbe63e752fcc0c808d2fb20a06a88e
publicationDate 2017-06-16-04:00^^<http://www.w3.org/2001/XMLSchema#date>
publicationNumber CN-206256006-U
titleOfInvention A kind of processing unit (plant) of borneol
abstract The utility model provides a kind of processing unit (plant) of borneol, including the first fractionating column, the middle part of the first fractionating column is connected with storage tank for turpentine oil by oil pump, oil pump the turpentine oil in storage tank for turpentine oil is pumped into the first fractionating column, the top of the first fractionating column connects firpene tank by Oil/Gas Pipe after the first condenser, firpene tank is connected by pipeline with esterification pot, esterification pot is connected by pipeline with after-fractionating tower, the bottom of after-fractionating tower connects crystallization case by pipeline, return duct is connected with the top of after-fractionating tower, return duct in extending into after-fractionating tower again after the second condenser.The processing unit (plant) extracts borneol has the advantages that time-consuming short, recovery rate is high.
priorityDate 2016-11-24-04:00^^<http://www.w3.org/2001/XMLSchema#date>
type http://data.epo.org/linked-data/def/patent/Publication

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