| Predicate |
Object |
| assignee |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_69c5c3393fae859639fdc9b8f3bc66af |
| classificationCPCAdditional |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/Y10S435-819
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/Y10S435-813
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/Y10S435-818
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2219-00085 |
| classificationCPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C12M41-32
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J19-1837
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C12P19-06
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C12M27-02
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C12P7-58
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C12M23-06
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J19-0053
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C12M41-00 |
| classificationIPCAdditional |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C12R1-01 |
| classificationIPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C12P1-00
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C12M1-00
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C12P7-00
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C12M1-02
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C12M1-08
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C12P19-06
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C12N1-00
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J19-18
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C12P7-58
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C12M1-40
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C12M1-36 |
| filingDate |
1985-11-07-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationDate |
1986-05-15-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber |
IE-852782-L |
| titleOfInvention |
Microbiological or enzymic reactor |
| abstract |
To improve the yield and/or reduce the energy cost in carrying out a microbiological or enzymatic process in a reactor and to make the reaction conditions essentially independent of the size of the reactor, it is proposed to make use, as a reactor, of an endless circulation tube in which the reaction components are circulated essentially according to a plug flow and in this process are fed through one or more in-line mixers fitted inside the tube. This method and reactor are suitable in particular for the preparation by fermentation of polysaccharides, especially xanthan, in which water, a production medium containing one or more sugars and nutrient salts and an inoculating material of a suitable aerobic bacterium are introduced into the said reactor tube and exposed to fermentation with air being supplied. Preferably the concentration of a reaction component or a value derived therefrom is measured at at least one point and the reaction velocity is regulated on the basis of the said measurement within critical limits.n[US4935348A] |
| priorityDate |
1984-11-15-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type |
http://data.epo.org/linked-data/def/patent/Publication |