| Predicate |
Object |
| assignee |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_86560af6dd8efd9678af7eb441f776a0
http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_de759ee7dadedbc1f11e51269779e75d
http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_1c828d8368efeddb4a9cee2d93477e8a |
| classificationCPCAdditional |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2300-44
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/Y02P30-20
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/Y10T137-85986
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2300-1014 |
| classificationCPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G3-40
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10L1-026
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10L1-00
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G1-08
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/D21C3-20
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/D21C11-0007
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G1-083
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G1-047
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G1-02
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G1-002
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G1-04 |
| classificationIPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G1-04 |
| filingDate |
2012-07-03-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| inventor |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_d408cb398698e5cab7c6d0d25857c27a
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_a242030f31356b139b1a53a3e5f03c18 |
| publicationDate |
2013-01-10-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber |
WO-2013005104-A2 |
| titleOfInvention |
Methods and systems for processing plants and converting cellulosic residue to crude bio-oils |
| abstract |
A continuous flow wood processing technology for extracting lignin from woody plant material and converting the delignified cellulosic residue to crude bio- oils is provided. Wood is chipped before processing starts and fed into a lignin extractor. The lignin extractor uses ethanol at high temperatures to dissolve the lignin with counter current material contactors. The ethanol containing dissolved lignin is removed from the lignin extractor, the dissolved lignin recovered, the ethanol and residual heat being recycled into the lignin extractor. The delignified cellulosic pulp is removed from the lignin extractor and subjected to a milling operation to convert the pulp into a smooth sludge for entry to a bio-convertor by a super critical water process. The product from this convertor is hydrocarbon sludge with a principal component being a kerogen. In a separate process crude oil is extracted from this sludge and the residue is prepared as a high phosphate Fertilizer. |
| isCitedBy |
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-11656756-B2
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-11662899-B2
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-10538012-B2
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/WO-2019158752-A1
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-11254026-B2
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-11306264-B2
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/WO-2013066196-A1 |
| priorityDate |
2011-07-03-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type |
http://data.epo.org/linked-data/def/patent/Publication |