http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-8420838-B2
Outgoing Links
Predicate | Object |
---|---|
assignee | http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_adb0e564374fedf34b36103d36e6455a http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_36414eef0c2ac54e5f17782cf9d15acd http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_3ecb61893be08d64cc03963edc4d7409 http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_84c76e16282ab34d5d129fc61b1e9074 http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_1069245fa6846feee59224a5b8eac1cc |
classificationCPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D3-32 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D5-0063 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D3-14 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07D311-72 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D3-143 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/F25J3-02 |
classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07D311-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01D3-14 |
filingDate | 2010-10-25-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
grantDate | 2013-04-16-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
inventor | http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_bfdc7ac0e55876cd69548084b60ed12b http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_de0bb0b5da0958dc575064ce47bb9a2f http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_3e9528b59b88286fdc75dee58e71a421 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_74f2db2fbebdf25d1883abc94f71d6a1 |
publicationDate | 2013-04-16-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
publicationNumber | US-8420838-B2 |
titleOfInvention | Process for the rectification of mixtures of high-boiling air- and/or temperature-sensitive useful products |
abstract | According to the invention, a process for the rectification of mixtures of high-boiling air- and/or temperature-sensitive substances which require a high separation efficiency is proposed, in particular a process for the working-up of a VE- or VEA-containing product stream. The process is characterized in particular in that, in a first purification stage, low-boiling products and unspecified isomers of the useful product are separated from the product stream virtually without loss of useful product and that, in a second purification stage, the useful product is removed in a stream having a purity of >97% by weight and a further stream having a purity of >92% by weight. A preferred embodiment of the process serves for working up VEA, in which the loss of useful product in the first purification stage is less than 5%, based on that amount of VEA in the feed which is added to the purification stage per unit time. Furthermore, the first purification stage may comprise a rectification column ( 1 ), from the top ( 1 a ) of which the low-boiling products and the unspecified isomers of VEA are taken off, a stream containing the useful product in purified form being taken off at the side ( 15 ) and/or at the bottom ( 1 b ) of the column ( 1 ). |
isCitedBy | http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-2013292242-A1 |
priorityDate | 2004-08-19-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Total number of triples: 45.