Predicate |
Object |
classificationCPCAdditional |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07B2200-09 |
classificationCPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C17-269 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C17-20 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C21-073 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C17-26 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C17-275 |
classificationIPCAdditional |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07B61-00 |
classificationIPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C21-073 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C17-269 |
filingDate |
2012-05-30-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
publicationDate |
2014-08-21-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
publicationNumber |
JP-2014520109-A |
titleOfInvention |
Process for producing chlorinated and / or fluorinated propenes |
abstract |
Processes for producing chlorinated and / or fluorinated propenes provide good product yields with a beneficial impurity profile of the crude product. Conveniently, the process may be performed at a temperature below 600 ° C. or below 500 ° C. so as to save energy and / or at a higher pressure so that high throughput can also be achieved. . The use of a catalyst or initiator can provide a further improvement in conversion and selectivity because the molar ratio of the reactants can be adjusted. |
isCitedBy |
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/WO-2020171177-A1 http://rdf.ncbi.nlm.nih.gov/pubchem/patent/JP-2020132593-A http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-11312673-B2 |
priorityDate |
2011-06-08-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
type |
http://data.epo.org/linked-data/def/patent/Publication |