| Predicate |
Object |
| assignee |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_f4ae9a7cabbaffd6e553f574c4fc1af8 |
| classificationCPCAdditional |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/Y02P30-20
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2300-1014
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2300-1003
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2300-4018 |
| classificationCPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C12P5-02
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G1-04
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G1-047
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G1-00
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G1-02
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G1-042
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G1-065
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G1-10
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C12M43-02 |
| classificationIPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C12P5-02
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C12M1-00
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G1-06
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G1-10
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G1-02
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G1-04 |
| filingDate |
2017-10-18^^<http://www.w3.org/2001/XMLSchema#date> |
| grantDate |
2019-01-08^^<http://www.w3.org/2001/XMLSchema#date> |
| inventor |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_6008cae1484f8bd0222d2f45b548e56c |
| publicationDate |
2019-01-08^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber |
US-10174260-B2 |
| titleOfInvention |
Process and apparatus for producing liquid hydrocarbon |
| abstract |
A continuous process for converting carbonaceous material contained in one or more feedstocks into a liquid hydrocarbon product, said feedstocks including the carbonaceous material being in a feed mixture including one or more fluids, said fluids including water and further liquid organic compounds at least partly produced by the process in a concentration of at least 1% by weight, where the process comprises converting at least part of the carbonaceous material by pressurising the feed mixture to a pressure in the range 250-400 bar; heating the feed mixture to a temperature in the range 370-450° C., and maintaining said pressurized and heated feed mixture in the desired pressure and temperature ranges in a reaction zone for a predefined time; cooling the feed mixture to a temperature in the range 25-200° C. and expanding the feed mixture to a pressure in the range of 1-70 bar, thereby causing the carbonaceous material to be converted to a liquid hydrocarbon product and separating from the converted feed mixture a fraction comprising liquid hydrocarbon product. |
| priorityDate |
2011-06-10^^<http://www.w3.org/2001/XMLSchema#date> |
| type |
http://data.epo.org/linked-data/def/patent/Publication |