| Predicate |
Object |
| assignee |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_4346749e66e870e1aa782161cdc1168c |
| classificationCPCAdditional |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2-33
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B03C2201-18 |
| classificationCPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G45-00
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G45-58
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B03C1-02
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2-332
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G47-00
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B03C1-30
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2-342
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J35-0033
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B03C1-288
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J8-005
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J8-007
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J8-22
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J8-228 |
| classificationIPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J35-00
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J8-00
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J19-00
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C27-00 |
| filingDate |
2008-09-09-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| inventor |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_0df58ac7bc5634217e419bc081f01a4f
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_9238eee39fc639bf71928905da135f43
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_2dbe5a7b87395eb47730cb227d71270d
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_a15884fed79d2191fef7866f3174ed3c
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_851113b02fe104f0d319ff161e8861fa |
| publicationDate |
2010-06-16-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber |
EP-2195111-A1 |
| titleOfInvention |
Commercial fischer-tropsch reactor |
| abstract |
A catalytic reaction system comprising: a catalytic reactor fluidly connected with at least two slurry loops, wherein the reactor comprises at least as many reactor product outlets and at least as many slurry return inlets as slurry loops; wherein each slurry loop comprises a separation system comprising a separation system inlet, a separation system product outlet, and a concentrated catalyst slurry outlet; a slurry offtake fluidly connecting the separation system inlet with one of the reactor product outlets; and a slurry return fluidly connecting the separation system outlet with one of the slurry return inlets. The system may comprise at least three slurry loops. The system may comprise at least four slurry loops. A method for converting synthesis gas into liquid hydrocarbons via the catalytic reaction system in also disclosed. |
| priorityDate |
2007-09-10-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type |
http://data.epo.org/linked-data/def/patent/Publication |