http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CA-2496728-A1
Outgoing Links
| Predicate | Object |
|---|---|
| assignee | http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_7580a1cdb7bf704802f84446f901fbf7 |
| classificationCPCAdditional | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D2257-504 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D2257-304 |
| classificationCPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10L3-10 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10L3-102 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D53-1462 |
| classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10L3-10 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01D53-14 |
| filingDate | 2005-02-09-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| inventor | http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_17f14b0e8fae269958def692a54b9edd http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_1198cd877c2a73b6a24257cc87de2312 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_b8f81c342ceb07eccbb554b33f879dd7 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_447cc21fed5d5488d15c6e83f0b8703e |
| publicationDate | 2005-08-13-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber | CA-2496728-A1 |
| titleOfInvention | Natural gas treatment process with extraction of the solvent in the purified natural gas |
| abstract | The natural gas arriving via line 1 is deacidified by setting contact with a solvent in column C2. The solvent loaded with compounds acid is regenerated in zone R. The purified gas discharged through line 9 has a part of the solvent. The process makes it possible to extract the solvent contained in the purified gas. The purified gas is contacted in the zone ZA with a liquid non-aqueous ionic material having the general formula Q + A-, Q + denoting a cation ammonium, phosphonium and / or sulphonium, and A- denoting an anion likely to form a liquid salt. The purified gas depleted in solvent is discharged through the conduit 17. The ionic liquid loaded with solvent is regenerated by heating in the evaporation device DE. Solvent separated from liquid ionic in the DE device are recycled. |
| priorityDate | 2004-02-13-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Total number of triples: 124.