http://rdf.ncbi.nlm.nih.gov/pubchem/patent/JP-2004500474-A
Outgoing Links
| Predicate | Object |
|---|---|
| classificationCPCAdditional | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2300-1022 |
| classificationCPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2-32 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G57-00 |
| classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G11-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G45-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G35-04 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G57-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G50-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G2-00 |
| filingDate | 2001-03-30^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationDate | 2004-01-08^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber | JP-2004500474-A |
| titleOfInvention | Improved method of converting syngas to distillate fuel |
| abstract | An integrated method for producing a distillate fuel from syngas is disclosed. The synthesis gas is reacted under Fischer-Tropsch conditions to form a product stream comprising a naphtha fraction, a distillate fuel fraction, and a fraction containing primarily wax and heavy products. The wax fraction is subjected to a paragon process, and the light olefins resulting from this process are oligomerized to produce additional isoolefins, which are optionally reduced to produce isoparaffins. The naphtha and distillate fuels can be isolated from the isomerization step, and the wax and heavy fractions from the oligomerization step are recycled, if any, until disappearance. Preferably, a portion of the syngas used in Fischer-Tropsch chemistry is derived from natural gas. Natural gas and C 3 + products from the Fischer-Tropsch process is either produced or hydrogenated additional ethane and C 5 + fractions undergo molecular redistribution by optionally generate additional feedstock for the oligomerization process I do. Distillate fuels produced in this way have relatively high octane and / or cetane numbers and low levels of sulfur and nitrogen impurities. This method is advantageous over other methods because it requires significantly less hydrogen and can operate at much lower temperatures and pressures. |
| isCitedBy | http://rdf.ncbi.nlm.nih.gov/pubchem/patent/JP-2005528379-A http://rdf.ncbi.nlm.nih.gov/pubchem/patent/JP-4790987-B2 http://rdf.ncbi.nlm.nih.gov/pubchem/patent/JP-2008500419-A http://rdf.ncbi.nlm.nih.gov/pubchem/patent/JP-4748939-B2 |
| priorityDate | 2000-04-03^^<http://www.w3.org/2001/XMLSchema#date> |
| type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
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