http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-100447118-C
Outgoing Links
Predicate | Object |
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assignee | http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_ac31afbea1cbbb03498644721ffb4a62 |
classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C7-08 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C13-10 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C9-15 |
filingDate | 2005-11-16-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
grantDate | 2008-12-31-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
inventor | http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_454aab274b061f5bc22a00ba3deaf06a http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_706fe8b59545e654e1139626b0980cf5 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_148a6fa68d5baf4757bb73ec1eb71087 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_19cd5685b52dc009fb34539d72f9edd2 |
publicationDate | 2008-12-31-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
publicationNumber | CN-100447118-C |
titleOfInvention | Extraction and rectification separation method for normal hexane and methyl cyclopentane |
abstract | The present invention relates to a method for extracting, rectifying and separating hexane and methyl cyclopentane, which comprises: a raw material (industrial hexane) and extracting and rectifying solvent (dimethyl phthalate) are added to an extracting and rectifying tower according to a certain mixture ratio; after separation, high-purity hexane is generated at a tower top, and solvent (dimethyl phthalate and methyl cyclopentane) is generated at a tower kettle; materials at the tower is fed in a solvent regenerating tower for distillation operation, and a generating product at the tower top is methyl cyclopentane; the generating product (methyl cyclopentane) at the tower top is further purified to obtain high-purity methyl cyclopentane. The solvent (dimethyl phthalate) at the tower kettle is sent back to the extracting and rectifying tower to be recycled. The certain mixture ratio is: the quality flow ratio of the raw material to the solvent is 1 to (3 to 5). By using the present invention, methyl cyclopentane in the raw material can be recovered, the recovery rate is at least 90%, and the hexane product of which the purity is at least 98% can be obtained. The solvent (dimethyl phthalate) for extraction and rectification can be recycled. Compared with a conventional method, the product has the advantages of high purity, high recovery rate, low energy consumption and no environmental pollution. |
priorityDate | 2005-11-16-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Total number of triples: 24.