http://rdf.ncbi.nlm.nih.gov/pubchem/patent/EP-1911505-A1
Outgoing Links
Predicate | Object |
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assignee | http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_7580a1cdb7bf704802f84446f901fbf7 http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_80d21b615b5cbb00bb46fca529dc0ddc |
classificationCPCAdditional | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D2258-0233 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D2257-504 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/Y02E20-32 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/Y02A50-20 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/Y02C20-40 |
classificationCPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D53-1475 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D53-1425 |
classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01D53-14 |
filingDate | 2007-09-25-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
inventor | http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_cf6e5a98442ce55bcec75bc1a12ebfbd http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_bc6f9de6ffff8a12dbcd1e5f13050086 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_55d50669f3b30d0bc98c5287cdc8fdc2 |
publicationDate | 2008-04-16-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
publicationNumber | EP-1911505-A1 |
titleOfInvention | Process for the removal of CO2 including a thermally integrated regenerator |
abstract | The CO 2 contained in combustion fumes is captured by carrying out, in combination, at least the following steps: a) burning a fuel by producing combustion fumes, b) the fumes are brought into contact with an absorbent solution so as to produce fumes depleted in CO 2 and a solution loaded with CO 2 , c) regenerating the CO 2 -corrected solution in a thermal regeneration column (RE) so as to produce a regenerated absorbent solution and a CO 2 -rich gas effluent (5), d) said CO 2 -rich off-gas is cooled so as to obtain a CO 2 enriched gas fraction which is discharged, and a liquid fraction which is introduced at the top of the regeneration column (RE) as reflux (7) .n n n In addition, at least one of the following operations is performed in step d): i) cooling (C1) said gaseous effluent to an intermediate temperature so as to produce a liquid flow and a gaseous flow, then subcooling (C2) the gaseous flow so as to produce said gaseous fraction and said liquid fraction, said liquid flow and said liquid fraction being collected and then introduced at the top of the regeneration column (RE) as reflux (7), ii) heating (E3) said liquid fraction by heat exchange with said gaseous effluent, iii) heating (E4) said liquid fraction or said liquid flow by heat exchange with said combustion fumes. |
isCitedBy | http://rdf.ncbi.nlm.nih.gov/pubchem/patent/WO-2010071461-A1 http://rdf.ncbi.nlm.nih.gov/pubchem/patent/WO-2008144918-A1 http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-101778663-B http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-8388737-B2 |
priorityDate | 2006-10-11-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Total number of triples: 53.