http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-101948385-B

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classificationIPCInventive http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C67-04
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C69-14
filingDate 2010-07-12-04:00^^<http://www.w3.org/2001/XMLSchema#date>
grantDate 2013-12-11-04:00^^<http://www.w3.org/2001/XMLSchema#date>
inventor http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_7a5744bd2ed2e47992fb6dd637cd420d
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_648fbde9e9e71d24e62298384201a7cd
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publicationDate 2013-12-11-04:00^^<http://www.w3.org/2001/XMLSchema#date>
publicationNumber CN-101948385-B
titleOfInvention Method for composing butyl acetate
abstract The invention relates to a method for composing butyl acetate. The method comprises the following steps of: homodromous continuously passing liquid acetic acid and C4 olefin through three fixed bed reactors, wherein 20 to 50w% of C4 olefin is mixed with the acetic acid and then sent to 1# and 2# reactors and the other C4 olefin is mixed with the resultant from the 1# and 2# reactors and then sent to 3# reactor, using small part of resultant from the 3# reactor as the feeding material of a primary rectifying tower 4, recycling the other into an entry of the 3# reactor with a recycle ratio of 1 to 10, and using macroporous strongly acid cation exchange resin as the catalyst required by the reaction, wherein the materials are externally preheated, the reaction temperature is controlled in a range of 60 to 100 DEG C through sleeved cooling water, the feeding speed of acetic acid is 0.5-2h-1, the reaction pressure of the fixed bed is controlled in a range of 0.5 to 5 MPa and the reaction conversion rate of acetic acid is 65 to 90%.
priorityDate 2010-07-12-04:00^^<http://www.w3.org/2001/XMLSchema#date>
type http://data.epo.org/linked-data/def/patent/Publication

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