| Predicate |
Object |
| assignee |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_0efa077d881a96aeb1e29b21ef1bbb58 |
| classificationCPCAdditional |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/Y02P20-582 |
| classificationCPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C209-60 |
| classificationIPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C67-00
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J29-46
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C211-07
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C209-00
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07B61-00
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J29-88
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C211-02
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J29-86
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C209-60
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J29-04
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J29-00 |
| filingDate |
1987-10-05-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| inventor |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_9334e96ef42560136b13414a3d7d4997
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_63b90669a39af9101ba9fa36133846f6
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_d0e9762f5fee01a189bad79a2e343a62
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_5e28664a719d352b4ca0700b2fa5ddb6
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_91e97d2ac18b0bc266bd54661c15bb91 |
| publicationDate |
1988-04-13-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber |
EP-0263462-A2 |
| titleOfInvention |
Process for the manufacture of amines |
| abstract |
The application relates to a process for the preparation of amines from olefins and ammonia or primary or secondary amines at temperatures between 80 ° C and 400 ° C at pressures between 40 and 700 bar in the presence of a Cr-containing borosilicate or Cr-containing iron silicate zeolite of the Pentasil type as a catalyst. The amine obtained is separated off and the unreacted starting materials are returned.n n n The Cr content of the catalyst is advantageously between 0.05% and 10% by weight. |
| isCitedBy |
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-7074964-B2
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-1312110-C
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/DE-4206992-A1
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/EP-0431451-A3
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/EP-0431451-A2
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/EP-1462165-A1 |
| priorityDate |
1986-10-08-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type |
http://data.epo.org/linked-data/def/patent/Publication |