http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CZ-300865-B6
Outgoing Links
Predicate | Object |
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assignee | http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_67197fa3d9b639bb088abc017792ea4c |
classificationCPCAdditional | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/Y02E50-10 |
classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C12P7-10 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C12P19-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07D307-50 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C12S3-04 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C12S3-12 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C53-08 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C53-02 |
filingDate | 2005-11-21-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
inventor | http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_64701e1f68446adfd21466f21841b922 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_27306744698c5accc70ef054afeac7ce http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_389516908c84c72db0597182549b3236 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_6a231d91b2c325ae902194c856d033fa |
publicationDate | 2009-08-26-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
publicationNumber | CZ-300865-B6 |
titleOfInvention | The method of production of glucose, ethanol, furfural, furan, lignin, acetic acid and ants from renewable raw materials and equipment for its implementation |
abstract | The production of glucose, ethanol, furfural, furan, lignin, acetic acid, and ants from renewable raw materials is based on continuous thermal-pressure hydrolysis of disintegrated lignocellulosic and starch feedstocks, after which the hydrolysed material undergoes at least two-phase expansion to form a water-containing vapor phase , furfural, methanol, acetic acid and ant, and the liquid phase, containing both an aqueous solution of hydrolysis sugar and other soluble substances and, on the other hand, unreacted solid lignocellulosic residues which are separated by compression or by filtration and treated with cellulosic enzymes upon addition of water of simple sugars which, after separation of the undigested lignin together with the treated starch raw materials and the liquid phase of the solid-free hydrolysis sugar, undergoes amylolytic hydrolysis, after which the sugar solution is further processed and / or fermented as ethano to the ethano 1, which is concentrated and dewatered after yeast separation. The continuous thermo-pressure hydrolysis is carried out in two stages, namely in the first stage at a temperature of 150 to 185 degC and a pressure of 0.6 to 1.0 MPa at a hydromodule of 1: 4 and in the second stage at the addition of pressurized water at a temperature of 200 with a pressure of 1.6 to 3.3 MPa, with phosphoric, hydrochloric, or other suitable acid in the range of 0.1 to 1% by weight, based on the suspension, being simultaneously injected into the second hydrolysis stage with pressurized water. for a 1: 3 to 1: 4 hydromodule. The liquid phase after the first step of hydrolysis is separated and used as a raw material for fermentation to ethanol or furfural. |
isCitedBy | http://rdf.ncbi.nlm.nih.gov/pubchem/patent/EP-2420560-A1 http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-9695484-B2 http://rdf.ncbi.nlm.nih.gov/pubchem/patent/JP-2013112661-A http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CZ-304261-B6 http://rdf.ncbi.nlm.nih.gov/pubchem/patent/EP-2198035-B1 http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-9150937-B2 |
priorityDate | 2005-11-21-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Total number of triples: 59.