| Predicate |
Object |
| assignee |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_51caf932f4ff80f8bea0d54b8dfa07a6 |
| classificationCPCAdditional |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2219-00243
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2219-00006
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2219-0011
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2219-00103 |
| classificationCPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C67-04
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C67-055
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J10-007
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J19-2415
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J8-06 |
| classificationIPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C69-24
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C69-145
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C67-04
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J8-06
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J10-00
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J31-04
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07B41-12
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C69-025
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J19-24
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07B61-00 |
| filingDate |
2000-06-01-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| grantDate |
2003-03-11-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| inventor |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_0ce0c8644a57a636eba8d41186a6aec1
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_5d66653e08a86a66a9483ad216b65dbf |
| publicationDate |
2003-03-11-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber |
TW-523423-B |
| titleOfInvention |
Process for carrying out catalytic multiphase reactions, in particular vinylations of carboxylic acids |
| abstract |
A process for carrying out catalytic multiphase reactions in a tube reactor, wherein the catalyst is present in the continuous phase and at least one starting material is present in a dispersed phase and the loading factor B of the tube reactor is reactor is equal to or greater than 0.8. The process is suitable particularly for preparing vinyl esters by reaction of carboxylic acids with acetylene, and has industrial value for long-active catalyst and space-time yield. |
| isCitedBy |
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/TW-I452034-B |
| priorityDate |
1999-06-02-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type |
http://data.epo.org/linked-data/def/patent/Publication |