http://rdf.ncbi.nlm.nih.gov/pubchem/patent/SK-281144-B6
Outgoing Links
| Predicate | Object |
|---|---|
| assignee | http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_32c8fbdb0983e1e4a1746582585aad98 http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_98b1f404c75d2f47895d1a631d348066 |
| classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C67-08 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C67-03 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07B41-12 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C69-14 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C69-12 |
| filingDate | 1998-04-02-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| inventor | http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_2b4a506a58e38b3f554d0b61ceecc971 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_6c1b1e348d7a6386b8aa17fb34ccf2a4 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_b5c97c98f4b405edfd1033612ae4a00f http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_240e3c48e874cdba2e2e2bed0f7f7c40 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_1697cde3a9a35cb28919f137951ace8d http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_e89005b0d29eda714e5e2fc2a2dad32f http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_75beb0a48ee663280f63e5e8cca5acf5 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_2895cb7d3f7424f096f572146eb3dcec |
| publicationDate | 2000-12-11-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber | SK-281144-B6 |
| titleOfInvention | METHOD OF PRODUCING BUTYLACETATE AND DEVICE FOR IMPLEMENTING THIS METHOD |
| abstract | Production of butyl acetate by esterification of acetic acid with butanol in the presence of a solid acid catalyst while separating the components by distillation, in which acetic acid and butanol are reported in a molar ratio of 1: 1 to 1: 10, in a defined amount into a system in which the reaction and distillation separation take place in three zones. In the recreation zone, the reaction proceeds simultaneously with the distillation separation of the components with different boiling points. Only the distillation separation takes place in the upper separation zone and the lower separation zone, so that the volatile phase is separated in the upper separation zone and is separated into an aqueous and organic phase which returns to the reaction upon cooling to 5 to 80 ° C as reflux. The ratio of feed of feed to reaction with the reflux of the organic phase is 1: 1 to 1: 20 and the reflux reflux is 60 to 100% of the total organic phase divided and the butyl acetate is separated as a booster and the apparatus for its performance. à |
| priorityDate | 1998-04-02-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Total number of triples: 42.