| Predicate |
Object |
| assignee |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_7580a1cdb7bf704802f84446f901fbf7 |
| classificationCPCAdditional |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/Y02P20-10 |
| classificationCPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D3-009
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J8-0469
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C15-073
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C2-64
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D3-32
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J8-0492
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J8-02 |
| classificationIPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G7-00
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J19-24
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C41-42
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C15-073
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01D3-00
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C43-04
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C2-64
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01D3-26
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J8-04 |
| filingDate |
1996-07-23-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| inventor |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_02ffac34bcaa87d4819ef65b9499c2a0
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_ac1587395c6d18a54b66b06725e3124f
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_57a07f1ec338ca07fb1373f7a324244e
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_2d88ed61fc191837f28a88adaad08139
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_587dac6aaa4829480914a54b13cb7685 |
| publicationDate |
1997-02-19-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber |
KR-970005334-A |
| titleOfInvention |
Reactive Distillation Methods and Apparatus Using Liquid and Vapor Phase Particle Distribution |
| abstract |
The present invention is carried out in a reactive distillation zone comprising one or more catalyst zones adjacent to two distillation zones, where the distillation vapor is circulated from the bottom to the top in a manner that is not substantially in contact with the catalyst and the liquid is in the top distillation zone. From (5) to a zone substantially centered at the bottom of the catalyst zone, circulating without contacting the catalyst, and having a radius downstream of the catalyst zone by one or more means 20 for injection into the liquid distribution zone 8. After circulating in the direction, the method relates to a reactive distillation process in which the liquid is recovered in the lower distillation zone 14 by one or more liquid discharge means 19 by circulating through the catalyst layer 8 in the catalyst zone. The present invention also relates to reactive distillation. |
| priorityDate |
1995-07-24-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type |
http://data.epo.org/linked-data/def/patent/Publication |