| Predicate |
Object |
| assignee |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_7ab07e6fd3ec0599bfaeaf1f9b2f5742 |
| classificationCPCAdditional |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/Y02P70-10
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2219-00069
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2208-00203
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2208-00176
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2219-00058
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/Y02P20-10 |
| classificationCPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J8-0496
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J8-1836
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J8-20
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C1-041
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J8-0457
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J8-0453
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D3-009 |
| classificationIPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C1-04
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01D3-00
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J8-04
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J8-20
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J8-18 |
| filingDate |
2000-11-17-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| inventor |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_f5fd3dc945baf44e8205d9e017957cf5
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_c0e8cfd2b60262dd52fc4d0525c7aee2
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_d8c0183bba57e419181f59928ff70a3e
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_347e6a387a85f2232ca029bf5f9a7a99 |
| publicationDate |
2001-05-25-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber |
WO-0136066-A2 |
| titleOfInvention |
Catalytic distillation reactor |
| abstract |
An apparatus and method is disclosed for producing hydrocarbons according to the Fischer-Tropsch process. The apparatus comprises a catalytic distillation reactor where reactants are fed into the catalytic distillation reactor to undergo catalytic reaction to form hydrocarbons. Physical separation of the unreacted materials and products occurs simultaneously in the catalytic distillation reactor. The catalytic distillation reactor is divided into reaction chambers so as to optimize control of the reaction and the distribution of hydrocarbon products. External heat exchangers are provided for the recovery of the heat generated in the reaction. |
| isCitedBy |
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-7985777-B2
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/AP-3739-A
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-114100527-A
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-6864293-B2
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/EA-026636-B1
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/AU-2011322285-B2
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-9243189-B2
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/WO-2012056203-A3
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/WO-2012056203-A2 |
| priorityDate |
1999-11-17-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type |
http://data.epo.org/linked-data/def/patent/Publication |