| Predicate |
Object |
| assignee |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_50d62ace054de9352384e2c7cd9dda0e |
| classificationCPCAdditional |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2219-00051
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2219-3322
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2219-00164 |
| classificationCPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J19-1812
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J19-1806
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J19-2415
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C47-21
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C45-75
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J19-0013 |
| classificationIPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C47-21
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C45-75 |
| filingDate |
2016-09-30-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| grantDate |
2019-05-30-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| inventor |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_4b8e325142b69549f570476c13b5c8f0
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_692990590dc3622c3f3de73806e33543
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_1a425f9325644a99db5834afb1bc6d3b
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_52d9a767a1415b31d3766ba148d60a8d
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_2573f69b0edeb56e9db40e5df15dd100 |
| publicationDate |
2019-05-30-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber |
ES-2714899-T3 |
| titleOfInvention |
Continuous production method for 2-Methylene Alkanes |
| abstract |
Method for the production of 2-methylene-alkanals of the general formula I ** Formula ** in which R1 represents an aliphatic moiety, by transforming alkanals according to general formula II ** Formula ** with an aqueous formaldehyde solution in the presence of at least one secondary amine, and at least one carboxylic acid, it is characterized in that the educts are reacted in a biphasic liquid / liquid system, and the reaction is carried out continuously within a Tubular reactor under laminar flow conditions with a Reynold number greater than or equal to 10 and less than or equal to 2320. |
| priorityDate |
2016-09-30-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type |
http://data.epo.org/linked-data/def/patent/Publication |