| Predicate |
Object |
| assignee |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_55bd9cdc5392138d8a2277d856d7a9e5 |
| classificationCPCAdditional |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C01B2203-025
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C01B2203-062
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C01B2203-061
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C01B2203-0495
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C01B2203-048
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C01B2203-0244
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10J2300-1659
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C01B2203-148
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C01B2203-146
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C01B2203-0475
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C01B2203-047
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C01B2203-0465
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C01B2203-043 |
| classificationCPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2-32
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10K1-32
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10K1-26
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C01B3-36
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10K1-20
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C01B3-56
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10J3-00 |
| classificationIPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10K3-06
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10K1-00 |
| filingDate |
2009-02-20-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| inventor |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_021eb03ef302a403aefcc7ed65f699e8 |
| publicationDate |
2009-08-27-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber |
CA-2715922-A1 |
| titleOfInvention |
Systems and processes for processing hydrogen and carbon monoxide |
| abstract |
In various implementations, various feed gas streams which include hydrogen and carbon monoxide may be processed for conversion to product streams. For example, the feed gas stream may be processed using the Fisher-Tropsh process or a methanol synthesis process. Unconverted hydrogen and carbon monoxide can be recycled at high recovery and/or inert components removed to prevent build-up in the recycle system by using an arrangement of pressure swing adsorption systems designed to recover impure product gas streams. |
| priorityDate |
2008-02-20-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type |
http://data.epo.org/linked-data/def/patent/Publication |