| Predicate |
Object |
| assignee |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_dc45703f67bc72a6db582867886fd5d5
http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_ea14b5cbfb7d7586efe6e9ae1cffc6ab |
| classificationCPCAdditional |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/Y02E50-10 |
| classificationCPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C12P7-06
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C13K1-02
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C12M1-02 |
| classificationIPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C12P7-06
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C13K1-02
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C12M1-02 |
| filingDate |
2016-08-01-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| inventor |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_e11bc14844365252414651c175917c16
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_4003c2027a11a86493c41c007a3de960
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_201d0d74b1444350a6479ff8e40b3084
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_6b8956da709100abbb724a5fb8fb1d5a
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_ea4e61f8b8087779fde64adeab6e6e75
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_45d6a465f0d53723bae85af323dcdc20
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_fda1899f0bc03662bf9d896d9ca365d5 |
| publicationDate |
2018-02-08-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber |
JP-2018019613-A |
| titleOfInvention |
Ethanol production method |
| abstract |
The present invention provides a method for producing a lignocellulose-derived compound that is high-speed and high-yield and in which foaming is suppressed. The method for producing a lignocellulosic biomass-derived compound of the present invention comprises a first fermentation step in which fermentation is performed by fed-batch culture in which yeast is cultured while a saccharified solution derived from lignocellulosic biomass is added. A second fermentation step for stopping the addition of the saccharified solution when the added saccharified solution reaches a certain amount and performing fermentation by batch culture, and for the yeast in the first fermentation step The flow acceleration of the saccharified solution is adjusted according to the sugar consumption rate of the yeast, and the yeast sugar consumption rate is equal to or higher than the maximum sugar consumption rate at which no residual sugar is generated. It is below the speed. [Selection figure] None |
| priorityDate |
2016-08-01-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type |
http://data.epo.org/linked-data/def/patent/Publication |