| Predicate |
Object |
| assignee |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_4e7f0a8c59c9c301cca5d3533d016afd |
| classificationCPCAdditional |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2219-00869
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2219-00873
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2219-00835
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/B01J2219-2459
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2219-2458
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2219-2453
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2219-2462
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2219-00871
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2219-00867 |
| classificationCPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2-00
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/B01J19-0093
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J8-04 |
| classificationIPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G2-00
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J8-04
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J19-00
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J8-02
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J19-24 |
| filingDate |
2005-05-24^^<http://www.w3.org/2001/XMLSchema#date> |
| inventor |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_0f004f4da033a95e1b8593fc2d675ffd |
| publicationDate |
2008-02-06^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber |
BR-PI0512096-A |
| titleOfInvention |
process and plant to carry out fischer-tropsch synthesis in feed gas |
| abstract |
PROCESS, AND PLANT, TO PERFORM FISCHER-TROPSCH SYNTHESIS ON A POWER GAS Fischer-Tropsch synthesis is performed on a CO / H * 2 feed gas using a plurality of catalytic reactor compact modules (12) each defining reaction channels. catalytic 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 CO is converted. The gases are cooled (16) between successive stages to remove water vapor, 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, so that no more than 75% of the remaining carbon monoxide also undergoes conversion during the second stage. The deleterious effect of water vapor on the catalyst is thus suppressed, while the overall capacity of the plant (10) can be adjusted by closing modules at each stage while keeping the numbers equal. |
| priorityDate |
2004-06-16^^<http://www.w3.org/2001/XMLSchema#date> |
| type |
http://data.epo.org/linked-data/def/patent/Publication |