http://rdf.ncbi.nlm.nih.gov/pubchem/patent/EP-3848437-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/C10G2300-1014 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2300-1003 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/Y02P30-20 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2300-4018 |
| classificationCPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G1-10 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/C10G1-04 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G1-065 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C12P5-02 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/C12M43-02 |
| classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G1-10 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G1-06 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G1-02 |
| 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 | 2021-07-14-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber | EP-3848437-A1 |
| titleOfInvention | Process and apparatus 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 providing a feed mixture comprising said one or more carbonaceous feedstocks and a liquid organic compound comprising at least 5% by weight of the feed mixture. The feed mixture passes to a reaction zone, converting at least part of the one or more carbonaceous feedstocks in the feed mixture into a liquid hydrocarbon product by pressurizing the feed mixture to a pressure in the range of 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 said pressure and temperature ranges for a predefined time, hereby producing a converted feed mixture containing CO2. The converted feed mixture is cooled to a temperature in the range 25-200 °C to produce a cooled and converted feed mixture. The cooled and converted feed mixture is depressurized below the critical point of CO2 by expanding the cooled and converted feed mixture to a pressure in the range 1-70 bar, to become 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 at least part of the 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. |
| 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
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