| Predicate |
Object |
| assignee |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_ac7aea826a7347198b235c992084b8dd |
| classificationCPCAdditional |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/Y02C20-40
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D2259-124
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/Y02A50-20
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D2252-504
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D2257-504
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D2258-0283
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D2252-204 |
| classificationCPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D53-1475
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D53-1493
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D53-62
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D53-78
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D53-1425 |
| classificationIPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01D53-14 |
| filingDate |
2014-10-06-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| inventor |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_0e0341446a3fc320891bc6a2833b13f1
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_514baf673e027449be90704769475fbd
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_03ca5f6dc67cd9fe9451aa17a10a3453
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_3193293d58b7d6e6d4bda9037c47ced2
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_af9adfb75a270d9c927bee684e70f58e |
| publicationDate |
2016-08-25-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber |
US-2016243490-A1 |
| titleOfInvention |
Process for capturing co2 from a co2-containing gas stream involving phase separation of aqueous absorbent |
| abstract |
The present invention relates to a process for capturing CO 2 from a CO 2 —containing gas stream, comprising the steps of: (a) contacting a CO 2 -containing gas stream with a CO 2 -absorbing agent in an absorption step wherein the temperature of the CO 2 absorbing agent at the end of the absorption step is below the LCST of the CO 2 -absorbing agent at the end of the absorption step, resulting in absorption of CO 2 ; (b) increasing the temperature of the CO 2 -absorbing agent, wherein the temperature at the end of the desorption step is above the LCST of the CO 2 -absorbing agent at the end of the desorption step, resulting in the desorption of CO 2 ; wherein the CO 2 -absorbing agent is a thermoresponsive CO 2 -absorbing agent comprising an amine-containing component, a solute inorganic salt, and water. |
| priorityDate |
2013-10-07-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type |
http://data.epo.org/linked-data/def/patent/Publication |