| Predicate |
Object |
| assignee |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_29714b58e14eabfad6bbee29ffba8872
http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_fef5b6c1ea325a5e054ec1e70c9a982a
http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_a016595f7b21b939b061a545d8bf14f4
http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_d48943cbec25455fb8fc039b3fa9d8cc
http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_f85b86a82c785dd662ee66807e34263a |
| classificationCPCAdditional |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/Y02E50-10 |
| classificationCPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C08H8-00
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C08B37-0003
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C08B37-0057
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C12P19-02 |
| classificationIPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C9-00
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C1-207 |
| filingDate |
2010-12-17-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| inventor |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_80ba19745a4789693ecdc546ce5f3b3c
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_b822356dc878af59ed59db94626c77b9
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_83dd1f97d5af29bb1c6c9cfaf016693c
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_2d782e5219d0823f0162649a68ce2f11
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_159a3c8fdaa4622d0697a536c9684359 |
| publicationDate |
2011-10-20-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber |
US-2011257447-A1 |
| titleOfInvention |
Process for producing hydrocarbons from microbial lipids |
| abstract |
A process for producing hydrocarbons from microbial lipids is provided by contacting a feed comprising microbial lipids with a hydrogenation catalyst and hydrogen at a temperature in the range of from 250 to 380° C. and a total pressure in the range of from 20 to 160 bar (absolute), to obtain an effluent comprising paraffinic hydrocarbons and water; optionally separating a liquid stream rich in paraffinic hydrocarbons from the effluent; contacting the paraffinic hydrocarbons in the liquid stream rich in paraffinic hydrocarbons or the effluent comprising paraffinic hydrocarbons by contacting hydrogen and the liquid stream with hydroisomerisation catalyst at a temperature in the range of from 280 to 450° C. and a total pressure in the range of from 20 to 160 bar (absolute); and separating at least one product fraction from the product stream obtained, wherein the hydrogenation catalyst and/or the hydroisomerisation catalyst comprises a sulfided hydrogenation catalyst. |
| isCitedBy |
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-2012151832-A1
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-2012151831-A1
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-RE46747-E
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-2015031929-A1
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-2014357924-A1 |
| priorityDate |
2009-12-18-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type |
http://data.epo.org/linked-data/def/patent/Publication |