| Predicate |
Object |
| assignee |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_741b3f48ab49782c52ece3e3c73e3c35 |
| classificationCPCAdditional |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2219-00094
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2219-185 |
| classificationCPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/A61K31-718
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C08B30-16
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J19-242 |
| classificationIPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/A61K31-718
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J19-24
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C08B30-12
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C08B31-12
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C08B30-16
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/A61K31-715 |
| filingDate |
1997-10-08-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| grantDate |
1999-02-11-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| inventor |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_72ba82074f4b44dd7627decbd78923e0
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_9e78f97e46a23ecaefa52eed6ead1690
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_dad48641aa0f37e1d1fae5afba04dafe
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_405f06ae8e435ffca547034f38116b6e |
| publicationDate |
1999-02-11-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber |
DE-19744353-C1 |
| titleOfInvention |
Process for the continuous production of hydrolytically degraded, if necessary. substituted starch, use of the hydrolytically degraded starch and device for its production |
| abstract |
The invention relates to a method for the continuous production of hydrolytically broken down starch or hydrolytically broken down substituted starch products such as hydroxyethyl- or hydroxypropyl starch. The invention essentially consists of carrying out most of the hydrolytic breakdown in a pipe-shaped, temperature-controlled reactor (22) having no mixing elements. The remaining breakdown is carried out in one or more reactors (34-40) fitted with mixing elements (fine hydrolysis). The product obtained can be used both in the food industry and for medical purposes, especially as plasma diluent. |
| priorityDate |
1997-08-08-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type |
http://data.epo.org/linked-data/def/patent/Publication |