http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CA-2863900-A1
Outgoing Links
| Predicate | Object |
|---|---|
| assignee | http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_b992c5d82de52547ebdcd34887ee5462 |
| classificationCPCAdditional | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2300-4081 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/Y02P30-20 |
| classificationCPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G1-002 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G47-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J21-04 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J21-18 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G45-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G3-50 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J37-0009 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G3-46 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G3-48 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C08H8-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J23-866 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G65-12 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J37-20 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G65-043 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J23-883 |
| classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G3-00 |
| filingDate | 2013-02-26-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| inventor | http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_078bd971b6a7872c2e10da0cc42add39 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_67436b232fb47ee52c6ebcf7b9a0ea2d http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_01dfa7d43cbe5b89468a715439cf8698 |
| publicationDate | 2013-09-19-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber | CA-2863900-A1 |
| titleOfInvention | Optimized method for recycling bio-oils into hydrocarbon fuels |
| abstract | The present invention relates to a process for producing hydrocarbon products from a feedstock comprising at least one non-pretreated bio-oil, said feed being introduced into at least a first hydroreforming step in the presence of hydrogen and a catalyst. hydroreforming composition comprising at least one transition metal chosen from the elements of groups 3 to 12 of the periodic table and at least one support chosen from activated carbons, silicon carbides, silicas, transition aluminas and alumina silicas , zirconium oxide, cerium oxide, titanium oxide and transition metal aluminates, taken alone or as a mixture, to obtain at least one liquid effluent comprising at least one aqueous phase and at least one phase organic, a second step of hydrotreating and / or hydrocracking at least a portion of the organic phase of the effluent from the hydroreforming step to obtain an effluent h hydrocarbon, wherein at least a portion of the organic phase of the effluent from the hydroreforming step is recycled to the hydroreforming step, in admixture with said feed comprising at least one bio-oil, with a rate of of recycle equal to the ratio of the mass flow rate of said organic phase to the mass flow rate of the non-pretreated bio-oil of between 0.05 and 2 and in which the hydrocarbon effluent resulting from the hydrotreatment step and / or from hydrocracking is not recycled in said hydroreforming step. |
| priorityDate | 2012-03-12-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Total number of triples: 76.