http://rdf.ncbi.nlm.nih.gov/pubchem/patent/EP-3854862-A1
Outgoing Links
| Predicate | Object |
|---|---|
| assignee | http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_f4ae9a7cabbaffd6e553f574c4fc1af8 |
| classificationCPCAdditional | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2300-4018 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/Y02P30-20 |
| classificationCPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G1-10 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G1-042 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/C12P5-02 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G1-02 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G1-04 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G1-065 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C12M43-02 |
| classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G1-06 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G1-02 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G1-10 |
| filingDate | 2012-06-11-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| inventor | http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_6008cae1484f8bd0222d2f45b548e56c |
| publicationDate | 2021-07-28-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber | EP-3854862-A1 |
| titleOfInvention | Process for producing liquid hydrocarbons |
| abstract | The invention relates to a continuous process for converting one or more carbonaceous feedstocks into a liquid hydrocarbon product by converting at least part of the one or more carbonaceous feedstocks in the feed mixture into a liquid hydrocarbon product. The feed mixture is pressurized to a pressure in the range 250-400 bar, heated 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, thereby producing a converted feed mixture containing CO2. The feed mixture is cooled to a temperature in the range 25-200 °C to produce a cooled and converted feed mixture and depressurized below the critical pressure of CO2 by expanding the cooled and converted feed mixture to a pressure in the range of 1-70 bar, to produce an expanded and cooled converted feed mixture. The expanded and cooled converted feed mixture is separated into a stream comprising the liquid hydrocarbon product and a water phase comprising liquid organic compounds which are water phase liquid organic compounds. At least part of the water phase liquid organic compounds is recovered from the water phase and at least part of the recovered water phase liquid organic compounds is added to the feed mixture. The stream comprising the liquid hydrocarbon product is heated to a temperature in the range 350-600°C, thereby producing at least one liquid hydrocarbon fraction and/or at least one solid fraction and/or at least one gas fraction and/or at least one aqueous fraction. |
| priorityDate | 2011-06-10-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Total number of triples: 129.