Predicate |
Object |
assignee |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_aa67eb74ea5b96d9f8f2cfdb3b025770 |
classificationCPCAdditional |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D2257-704 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D2256-22 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D2259-40001 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D2259-40086 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/Y10S62-928 |
classificationCPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D53-261 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D53-04 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B08B7-0021 |
classificationIPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C01B32-50 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01D53-04 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B08B7-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01D53-26 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01D11-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/F25J1-00 |
filingDate |
2003-10-02-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
inventor |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_c1a3fac5b5de7cbad34185350011265d http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_6b45232dfbc7897a935096ffb68d1d1b http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_d9a2d586e78a1397f5987bfa66b50797 |
publicationDate |
2004-08-01-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
publicationNumber |
TW-200413079-A |
titleOfInvention |
CO2 recovery process for supercritical extraction |
abstract |
A carbon dioxide recovery apparatus (1) and process for supercritical extraction includes providing a process stream (61) from a supercritical extraction procedure (60) in which the process stream (61) includes pressurized carbon dioxide, extraction process waste and optionally at least one co-solvent; reducing the pressure of the process stream below critical pressure; venting low pressure carbon dioxide vapor (66) to exhaust; cooling the process stream to form a two phase mixture; separating the two phase mixture into a process liquid (71), containing co-solvent if present, and a process vapor phase stream (72); collecting the process liquid; filtering the process vapor phase stream (72) to remove particulates and optionally residual co-solvent; passing the filtered process vapor stream (81) through an adsorber (85) to remove trace impurities to form a purified carbon dioxide vapor stream (90); and, drying the purified carbon dioxide vapor stream (90) to remove residual water vapor. |
priorityDate |
2002-10-02-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
type |
http://data.epo.org/linked-data/def/patent/Publication |