http://rdf.ncbi.nlm.nih.gov/pubchem/patent/KR-100909641-B1
Outgoing Links
| Predicate | Object |
|---|---|
| classificationCPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C7-12 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C13-16 |
| classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C13-16 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C7-12 |
| filingDate | 2006-03-01-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| grantDate | 2009-07-27-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationDate | 2009-07-27-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber | KR-100909641-B1 |
| titleOfInvention | Product recovery from improved simulated moving bed adsorption |
| abstract | The product purity from the simulated mobile bed adsorptive separation process or the throughput of the simulated mobile bed adsorptive separation process is used to separate the desorbent (D) from the adsorption chambers (100, 200), preferably from the raffinate product (RP). Incremental by flushing the contents of the transfer line 10 previously used to remove the raffinate stream into the nate column 400. Preferably the stream from the adsorption chamber is used as the flushing liquid at the midpoint between the feed access point and the raffinate withdrawal. This flushing step is carried out during the transfer line flush period, or when the process conduits are then used to fill the feed stream F into the adsorption chambers 100 and 200, the adsorption chambers 100 and 200 of the amount of raffinate material. It prevents you from moving inside. n n Simulated moving bed adsorption, product recovery, flushing |
| priorityDate | 2005-03-03-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Total number of triples: 29.