| Predicate |
Object |
| assignee |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_4e7f0a8c59c9c301cca5d3533d016afd |
| classificationCPCAdditional |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2219-0002
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2219-2479
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2219-00835
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2219-00873
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2219-00867
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2219-00869
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2219-2459
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2219-2462
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2219-2458
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2219-00871
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2219-2453 |
| classificationCPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J8-02
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J19-249
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2-341
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2-00
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J8-04
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J19-0093 |
| classificationIPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G2-00
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J19-00
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J8-04
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J19-24
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J8-02 |
| filingDate |
2005-05-24-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| grantDate |
2012-05-22-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| inventor |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_8f0573b364881565320dc392030a6c7c |
| publicationDate |
2012-05-22-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber |
CA-2568702-C |
| titleOfInvention |
Catalytic plant and process for performing fischer-tropsch synthesis |
| abstract |
Fischer-Tropsch synthesis is performed on a CO/H*2 feed gas using a plurality of compact catalytic reactor modules (12) each defining catalytic reaction channels and coolant channels, in two successive stages, with the same number of reactor modules for each stage. The gas flow velocity in the first stage is sufficiently high that no more than 75% of the CO undergoes conversion. The gases are cooled (16) between successive stages so as to remove water vapour, and the pressure is reduced (20) before they are subjected to the second stage. In addition the reaction temperature for the second stage is lower than for the first stage, such that no more than 75% of the remaining carbon monoxide undergoes conversion during the second stage too. The deleterious effect of water vapour on the catalyst is hence suppressed, while the overall capacity of the plant (10) can be adjusted by closing off modules in each stage while keeping the numbers equal. |
| priorityDate |
2004-06-16-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type |
http://data.epo.org/linked-data/def/patent/Publication |