http://rdf.ncbi.nlm.nih.gov/pubchem/patent/WO-2013087942-A1
Outgoing Links
| Predicate | Object |
|---|---|
| assignee | http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_70ec63d39d6704bacc5c7068c93ded43 http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_50907fc1b392e2bf592f74fb8123032d |
| classificationCPCAdditional | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2400-08 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2400-06 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2400-04 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2300-1025 |
| classificationCPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G45-02 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10L1-04 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G55-02 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G47-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G65-14 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2-332 |
| classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G2-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G47-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G45-02 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G65-14 |
| filingDate | 2012-12-17-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| inventor | http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_1f71fb9285b206d8c465918045d496dc http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_a72f64c367912d3b7a67eb8a6f7aa606 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_3a31170c8ac980c18cd5d9842ce38f25 |
| publicationDate | 2013-06-20-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber | WO-2013087942-A1 |
| titleOfInvention | Integrated gas-to-liquid condensate process and apparatus |
| abstract | A process is provided for production of a middle distillate fraction from a gas-to-liquid (GTL) conversion comprising the steps of: (a) providing a feed stream comprising a natural gas and a condensate and separating a condensate from the natural gas feed stream to produce a condensate feed stream and a natural gas feed stream; (b) preparing a mixture of carbon monoxide and hydrogen from the natural gas feed stream obtained in step (a); (c) preparing a long chain hydrocarbon product stream by performing a Fischer-Tropsch reaction using carbon monoxide and hydrogen obtained in step (b); (d) Subjecting the long chain hydrocarbon product stream to a hydrocracking/hydroisomerization step to obtain a hydrocracked/hydroisomerised Fischer-Tropsch (FT) product stream; (e) treating the condensate stream of step (a) with a desulfurization step to generate a condensate product stream; (f) combining the hydrocracked/hydroisomerised FT product stream of step (d) with the condensate product stream of step (e) in order to provide a distillation feed stream; and (g) performing a distillation step on the distillation feed stream, wherein the distillation step provides for isolation of middle distillate products; wherein the steps (c) to (d) occur substantially concurrently with step (e). Middle distillate fractions and fuel/fuel blends obtained according to the process are also provided. |
| isCitedBy | http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-108003939-A http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-2021403816-A1 http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-2022098501-A1 |
| priorityDate | 2011-12-16-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Total number of triples: 48.