Predicate |
Object |
assignee |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_f2d13079288b02b1acb0beb05d381467 |
classificationCPCAdditional |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2300-4006 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2300-4043 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/Y02P30-40 |
classificationCPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2-332 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2-50 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2-30 |
classificationIPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G2-00 |
filingDate |
2015-03-19-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
inventor |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_7228082f74ae9bf9b326326a3981b805 |
publicationDate |
2015-10-01-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
publicationNumber |
CA-2941105-A1 |
titleOfInvention |
A fischer-tropsch synthesis process |
abstract |
A Fischer-Tropsch synthesis process (10) includes feeding gaseous reactants (20) including at least CO, H2 and C02 into a reactor (14) holding an iron-based catalyst. The H2 and CO are fed in a H2:CO molar ratio of at least 2: 1 and the C02 and CO are fed in a C02:CO molar ratio of at least 0.5: 1. The reactor (14) is controlled at an operating temperature in the range from about 260°C to about 300°C. A liquid product (22) and a gaseous product (24) including hydrocarbons, CO, H2, water and C02 are withdrawn from the reactor (14). |
priorityDate |
2014-03-24-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
type |
http://data.epo.org/linked-data/def/patent/Publication |