http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-204522355-U
Outgoing Links
| Predicate | Object |
|---|---|
| assignee | http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_bcf1685a830b43f1c785869c22a554ca |
| classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01D3-14 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C15-04 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C13-20 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C7-04 |
| filingDate | 2015-02-06-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| grantDate | 2015-08-05-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| inventor | http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_a1f9c9219fa09e405901155991f4f421 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_2b02c6827bf550dfe34d3c6224c91cb0 |
| publicationDate | 2015-08-05-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber | CN-204522355-U |
| titleOfInvention | Adopt the device of rectifying tower with bulkhead Separation of Benzene or separating cyclohexene |
| abstract | The utility model relates to a kind of device adopting rectifying tower with bulkhead Separation of Benzene or separating cyclohexene, primarily of rectifying tower with bulkhead, separation condenser, separation return tank, is separated reflux pump, recovery condenser, recovery return tank, recovery reflux pump, tower reactor pump, solvent cooler, reboiler composition.Existing benzene knockout tower and benzene recovery tower merge by this device, and benzene separation and benzene recovery etc. operate in a rectifying tower with bulkhead with one section of longitudinal baffle to be carried out; Cyclohexene knockout tower and cyclohexene recovery tower merge, and cyclohexene separation and cyclohexene recovery etc. operate in a rectifying tower with bulkhead with one section of longitudinal baffle to be carried out.Compare with traditional extraction rectification technique, rectifying tower with bulkhead technique can reduce the energy consumption of about 20% and the investment cost of about 25%.The utility model reduces the back-mixing of intermediate species and has increased substantially the thermodynamic efficiency of process, decreases energy ezpenditure and number of devices and investment, thus reduces production cost. |
| priorityDate | 2015-02-06-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Total number of triples: 27.