http://rdf.ncbi.nlm.nih.gov/pubchem/patent/SU-1057490-A1
Outgoing Links
| Predicate | Object |
|---|---|
| assignee | http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_0cfa5a30de245d361de1f9b0e0e122e1 |
| classificationIPCAdditional | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/G05D27-00 |
| classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C47-00 |
| filingDate | 1982-05-24-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| grantDate | 1983-11-30-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| inventor | http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_4aa25cf2bda12b997513b56e05261ba0 |
| publicationDate | 1983-11-30-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber | SU-1057490-A1 |
| titleOfInvention | Method for controlling condensation of butyric aldehyde |
| abstract | THE METHOD OF MANAGING THE PROCESS OF CONDENSING OIL ALDEHYDE in a reactor containing successively connected mixers, heaters, coolers and coils, by adjusting the temperature of the reaction mixture after the heater by varying the steam flow rate to the heater and the temperature of the reaction mixture after the 5 coolers, changing the flow rate of the mixture after the heater, and changing the flow rate of the reaction mixture after the refrigerator. that, in order to increase the yield of the target product, additionally regulate the consumption of recycled catalyst depending on the costs of raw materials and catalyst and temperature profile of the reaction zone of the reactor. h (L cz SP 4 CO |
| priorityDate | 1982-05-24-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Total number of triples: 16.