http://rdf.ncbi.nlm.nih.gov/pubchem/patent/RU-2012156250-A
Outgoing Links
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classificationCPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G3-49 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G3-50 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J21-04 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J23-888 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G3-54 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/C10L1-08 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10L1-06 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10L1-04 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G49-04 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G45-60 |
classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G3-00 |
filingDate | 2011-05-23-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
publicationDate | 2014-06-27-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
publicationNumber | RU-2012156250-A |
titleOfInvention | METHOD AND DEVICE FOR PRODUCING FUEL FROM RAW MATERIALS BY BIOLOGICAL ORIGIN BY ONE-STAGE HYDROGENING IN THE PRESENCE OF NIW CATALYST |
abstract | 1. A method of obtaining a mixture of fuel components, characterized in that the method includes providing raw materials of biological origin selected from tall oil, crude tall oil, resins and resin acids obtained from plants, and bio-oil from hydrolyzed wood; one-stage hydrogenation of said raw materials of biological origin and gaseous hydrogen in the presence of a catalyst system comprising a NiW catalyst supported on zeolite-AlO to form a mixture of fuel components. 2. The method according to claim 1, characterized in that the catalyst is diluted with silicon carbide, alumina, glass beads, a less active similar catalyst and / or inert ingredients. The method according to claim 1, characterized in that the catalytic system includes at least one protective layer. The method according to claim 1, characterized in that additional sulfur is supplied to the hydrogenation step. The method according to claim 1, characterized in that the hydrogen is recovered and returned back to the hydrogenation step. The method according to claim 1, characterized in that part of the mixture of fuel components is returned back to raw materials of biological origin and / or to the hydrogenation step. The method according to claim 1, characterized in that the hydrogenation step is carried out at a temperature in the range of from about 280 ° C to about 500 ° C, preferably from about 330 ° C to about 430 ° C. The method according to claim 1, characterized in that the hydrogenation step is carried out at a pressure of from about 30 to about 200 bar, preferably at a pressure of from about 70 to about 100 bar, most preferably from about 50 to about 90 bar. Spo |
priorityDate | 2010-05-25-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Total number of triples: 41.