| Predicate |
Object |
| assignee |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_bd1af66b7a51d0eca8584ed9f5ffad3b
http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_47d1736bf3917c4bced8a0bd6a884413
http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_261e198ec49c4ef25efbd06f57e2194c
http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_21cc990a52245071ea2f6cd10c126b30
http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_a2a99738c564d0d4da77d442ec8f7500 |
| classificationCPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2-32
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J12-00
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2-50 |
| classificationIPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C27-00
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J12-00 |
| filingDate |
2012-10-04-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| inventor |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_622bb302fb05eee5343fd569f145fc4b
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_5b36c75e808a8fb419ecd81262aaed4a
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_90ff40efdce0f8d3fc2a6d70b4c85e6a
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_d693d23e9ff666f82615177e8c0313b8 |
| publicationDate |
2014-04-10-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber |
US-2014100295-A1 |
| titleOfInvention |
Process and system for producing synthetic crude oil from offshore produced fluids containing high co2 content |
| abstract |
A system and process for producing synthetic crude oil from produced fluids of an oil well is disclosed. The system comprises a separation plant for producing an associated gas stream from produced fluids a membrane unit comprising a plurality of polymer membranes to provide a CO 2 enriched permeate stream and a CO 2 depleted product gas stream, a gas conversion plant for converting the CO 2 depleted product gas stream into a synthetic crude oil and a heat exchanger adding heat to the associated gas stream so that the membrane unit operates at a temperature of at least 80° C. during separation of the associated gas stream using the membrane unit. A process using the aforementioned components, including separation of the associated gas stream using the membrane unit at a temperature >80° C., into a CO 2 enriched stream and a CO 2 depleted product stream, is also described. |
| isCitedBy |
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/KR-20180100108-A
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-2018290124-A1
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/WO-2017062721-A1
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/KR-102406063-B1
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-108698951-A
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-10688466-B2 |
| priorityDate |
2011-10-04-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type |
http://data.epo.org/linked-data/def/patent/Publication |