Predicate |
Object |
assignee |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_9aa697692734f1f3df89fd278db976cb http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_74973199515dbabd2310245aab03e282 |
classificationCPCAdditional |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/Y02C20-40 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D2251-80 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D53-77 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D2257-504 |
classificationCPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D53-1475 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D53-62 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D53-1412 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D53-1425 |
classificationIPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01D53-96 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01D53-78 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01D53-62 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01D53-18 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C01B32-50 |
filingDate |
2009-12-23^^<http://www.w3.org/2001/XMLSchema#date> |
inventor |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_078977b4c1bdd0c10740b7d607bc9959 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_c6d21082c3c60c688f316e5a2b6eabfd http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_e3ab93ba80edb74cd21361f2d7516774 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_d9fa4fd3d76614a5e5a2a78a71b52ab2 |
publicationDate |
2010-12-23^^<http://www.w3.org/2001/XMLSchema#date> |
publicationNumber |
US-2010319532-A1 |
titleOfInvention |
Co2 recovery apparatus and co2 recovery method |
abstract |
Provided are a CO 2 absorber that reduces CO 2 contained in flue gas; a regenerator that reduces CO 2 contained in rich solvent absorbing CO 2 to regenerate the rich solvent, so that lean solvent having the CO 2 reduced in the regenerator is reused in the CO 2 absorber; a heat exchanger that allows the rich solvent to exchange heat with the lean solvent; and a controller that controls to extract rich solvent portion that is part of the rich solvent, to allow the rich solvent portion to by pass the heat exchanger, and to be supplied into the top of the regenerator without exchanging heat so as to minimize a sum of an enthalpy that is taken out of the regenerator as CO 2 gas accompanying steam and an enthalpy of the lean solvent after heat exchange with the rich solvent in the heat exchanger. |
isCitedBy |
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-10005032-B2 http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-109351125-A http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-105664674-A http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-2014301928-A1 http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-9815016-B2 http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-2018216532-A1 http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-2013233015-A1 http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-11229873-B2 http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-112996587-A http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-9314741-B2 http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-9339762-B2 |
priorityDate |
2009-06-17^^<http://www.w3.org/2001/XMLSchema#date> |
type |
http://data.epo.org/linked-data/def/patent/Publication |